diff --git a/.gitattributes b/.gitattributes new file mode 100644 index 00000000..98b36c22 --- /dev/null +++ b/.gitattributes @@ -0,0 +1,3 @@ +*.JPG filter=lfs diff=lfs merge=lfs -text +*.ttf filter=lfs diff=lfs merge=lfs -text +*.png filter=lfs diff=lfs merge=lfs -text diff --git a/docs/.fonts/Carlito-Bold.ttf b/docs/.fonts/Carlito-Bold.ttf new file mode 100644 index 00000000..b25a872e --- /dev/null +++ b/docs/.fonts/Carlito-Bold.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:0f62ab34ad5d079a0a28fac01bcf7c7a724a4db4d6cb99cab9cabff382fbb80f +size 690516 diff --git a/docs/.fonts/Carlito-BoldItalic.ttf b/docs/.fonts/Carlito-BoldItalic.ttf new file mode 100644 index 00000000..383e98c6 --- /dev/null +++ b/docs/.fonts/Carlito-BoldItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:380764b6898d7b73ceae6384b2958b196d2a0428962ef3adf138d27947228666 +size 816716 diff --git a/docs/.fonts/Carlito-Italic.ttf b/docs/.fonts/Carlito-Italic.ttf new file mode 100644 index 00000000..c4360a17 --- /dev/null +++ b/docs/.fonts/Carlito-Italic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:718a0663864d37a4868220a19b9668a5fe10a46197f6df367b4c2c30c04c026c +size 623416 diff --git a/docs/.fonts/Carlito-Regular.ttf b/docs/.fonts/Carlito-Regular.ttf new file mode 100644 index 00000000..f3adec06 --- /dev/null +++ b/docs/.fonts/Carlito-Regular.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:b4ff23ba370cc95a3c349336b73f9c28514a1371210f89832efc85c4b1ea7131 +size 635996 diff --git a/docs/.fonts/OFL.txt b/docs/.fonts/OFL.txt new file mode 100644 index 00000000..da31af08 --- /dev/null +++ b/docs/.fonts/OFL.txt @@ -0,0 +1,93 @@ +Copyright 2020 The Poppins Project Authors (https://github.com/itfoundry/Poppins) + +This Font Software is licensed under the SIL Open Font License, Version 1.1. +This license is copied below, and is also available with a FAQ at: +https://openfontlicense.org + + +----------------------------------------------------------- +SIL OPEN FONT LICENSE Version 1.1 - 26 February 2007 +----------------------------------------------------------- + +PREAMBLE +The goals of the Open Font License (OFL) are to stimulate worldwide +development of collaborative font projects, to support the font creation +efforts of academic and linguistic communities, and to provide a free and +open framework in which fonts may be shared and improved in partnership +with others. + +The OFL allows the licensed fonts to be used, studied, modified and +redistributed freely as long as they are not sold by themselves. The +fonts, including any derivative works, can be bundled, embedded, +redistributed and/or sold with any software provided that any reserved +names are not used by derivative works. The fonts and derivatives, +however, cannot be released under any other type of license. The +requirement for fonts to remain under this license does not apply +to any document created using the fonts or their derivatives. + +DEFINITIONS +"Font Software" refers to the set of files released by the Copyright +Holder(s) under this license and clearly marked as such. This may +include source files, build scripts and documentation. + +"Reserved Font Name" refers to any names specified as such after the +copyright statement(s). + +"Original Version" refers to the collection of Font Software components as +distributed by the Copyright Holder(s). + +"Modified Version" refers to any derivative made by adding to, deleting, +or substituting -- in part or in whole -- any of the components of the +Original Version, by changing formats or by porting the Font Software to a +new environment. + +"Author" refers to any designer, engineer, programmer, technical +writer or other person who contributed to the Font Software. + +PERMISSION & CONDITIONS +Permission is hereby granted, free of charge, to any person obtaining +a copy of the Font Software, to use, study, copy, merge, embed, modify, +redistribute, and sell modified and unmodified copies of the Font +Software, subject to the following conditions: + +1) Neither the Font Software nor any of its individual components, +in Original or Modified Versions, may be sold by itself. + +2) Original or Modified Versions of the Font Software may be bundled, +redistributed and/or sold with any software, provided that each copy +contains the above copyright notice and this license. These can be +included either as stand-alone text files, human-readable headers or +in the appropriate machine-readable metadata fields within text or +binary files as long as those fields can be easily viewed by the user. + +3) No Modified Version of the Font Software may use the Reserved Font +Name(s) unless explicit written permission is granted by the corresponding +Copyright Holder. This restriction only applies to the primary font name as +presented to the users. + +4) The name(s) of the Copyright Holder(s) or the Author(s) of the Font +Software shall not be used to promote, endorse or advertise any +Modified Version, except to acknowledge the contribution(s) of the +Copyright Holder(s) and the Author(s) or with their explicit written +permission. + +5) The Font Software, modified or unmodified, in part or in whole, +must be distributed entirely under this license, and must not be +distributed under any other license. The requirement for fonts to +remain under this license does not apply to any document created +using the Font Software. + +TERMINATION +This license becomes null and void if any of the above conditions are +not met. + +DISCLAIMER +THE FONT SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, +EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED TO ANY WARRANTIES OF +MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT +OF COPYRIGHT, PATENT, TRADEMARK, OR OTHER RIGHT. IN NO EVENT SHALL THE +COPYRIGHT HOLDER BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, +INCLUDING ANY GENERAL, SPECIAL, INDIRECT, INCIDENTAL, OR CONSEQUENTIAL +DAMAGES, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING +FROM, OUT OF THE USE OR INABILITY TO USE THE FONT SOFTWARE OR FROM +OTHER DEALINGS IN THE FONT SOFTWARE. diff --git a/docs/.fonts/Poppins-Black.ttf b/docs/.fonts/Poppins-Black.ttf new file mode 100644 index 00000000..88c10807 --- /dev/null +++ b/docs/.fonts/Poppins-Black.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:291e4388a436cf0c0d532ce4735a4ca36bd2286912b051ea423d5c383be06cd7 +size 151396 diff --git a/docs/.fonts/Poppins-BlackItalic.ttf b/docs/.fonts/Poppins-BlackItalic.ttf new file mode 100644 index 00000000..0b68f855 --- /dev/null +++ b/docs/.fonts/Poppins-BlackItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:a5e3e31e9dc6878269fdda8a968f8c0212beef9f7ef6028b6d1e02293316db7d +size 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--git a/docs/.fonts/Poppins-ExtraBoldItalic.ttf b/docs/.fonts/Poppins-ExtraBoldItalic.ttf new file mode 100644 index 00000000..68a3d95f --- /dev/null +++ b/docs/.fonts/Poppins-ExtraBoldItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:bba986e116690660f70d3ebb18a74d8d2c8eafcda6c28c8ffc4306aa1e2b91e4 +size 173916 diff --git a/docs/.fonts/Poppins-ExtraLight.ttf b/docs/.fonts/Poppins-ExtraLight.ttf new file mode 100644 index 00000000..3aaccd31 --- /dev/null +++ b/docs/.fonts/Poppins-ExtraLight.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:60c4bb1b8f272f0ac4702b962cc46e58e885a65624479be1c0646c9e37d9ce62 +size 161456 diff --git a/docs/.fonts/Poppins-ExtraLightItalic.ttf b/docs/.fonts/Poppins-ExtraLightItalic.ttf new file mode 100644 index 00000000..65186417 --- /dev/null +++ b/docs/.fonts/Poppins-ExtraLightItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:05418f4d333f25ddaf359adaf39b2777e64dad0f83c3fa4502d193d0ad19a9b7 +size 186168 diff --git a/docs/.fonts/Poppins-Italic.ttf b/docs/.fonts/Poppins-Italic.ttf new file mode 100644 index 00000000..ca23a78b --- /dev/null +++ b/docs/.fonts/Poppins-Italic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:3225cec6a018310497ea9ee116aa43b2a833464fed6156dceb9a3a4424bb8613 +size 182012 diff --git a/docs/.fonts/Poppins-Light.ttf b/docs/.fonts/Poppins-Light.ttf new file mode 100644 index 00000000..656ac62e --- /dev/null +++ b/docs/.fonts/Poppins-Light.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:647f014d36822ef7e0413ffbb65598ae0cb57fb798e635c63912c93d94eb356a +size 159892 diff --git a/docs/.fonts/Poppins-LightItalic.ttf b/docs/.fonts/Poppins-LightItalic.ttf new file mode 100644 index 00000000..94e77c8e --- /dev/null +++ b/docs/.fonts/Poppins-LightItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:6d00aa5531c8b8ba0934de7925985c6636c99fbc89b4c9f79629fb4a9067654f +size 184460 diff --git a/docs/.fonts/Poppins-Medium.ttf b/docs/.fonts/Poppins-Medium.ttf new file mode 100644 index 00000000..be10957d --- /dev/null +++ b/docs/.fonts/Poppins-Medium.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:8d909883de81344e0fbcfef30e931872e92d9aeecdf85b6dcf6e0b28c078e98e +size 156520 diff --git a/docs/.fonts/Poppins-MediumItalic.ttf b/docs/.fonts/Poppins-MediumItalic.ttf new file mode 100644 index 00000000..729cb196 --- /dev/null +++ b/docs/.fonts/Poppins-MediumItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:449f6bd907fe29dbdfd5ef0990bdbb7fd800efa748a83f7b7529dcb94f79955b +size 180444 diff --git a/docs/.fonts/Poppins-Regular.ttf b/docs/.fonts/Poppins-Regular.ttf new file mode 100644 index 00000000..9d6366e1 --- /dev/null +++ b/docs/.fonts/Poppins-Regular.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:707fdc5c8bab57a90061c6a8ed7b70d5ffb82fc810e994e79f90bace890c255a +size 158240 diff --git a/docs/.fonts/Poppins-SemiBold.ttf b/docs/.fonts/Poppins-SemiBold.ttf new file mode 100644 index 00000000..1610c642 --- /dev/null +++ b/docs/.fonts/Poppins-SemiBold.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:248c0244b350ec68880996aa6be6d7796274b49992d5fcbbefe251906aa4ea36 +size 155232 diff --git a/docs/.fonts/Poppins-SemiBoldItalic.ttf b/docs/.fonts/Poppins-SemiBoldItalic.ttf new file mode 100644 index 00000000..e3350480 --- /dev/null +++ b/docs/.fonts/Poppins-SemiBoldItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:74b31cbc29dc90c2d630e77673e7b6f714ff9bb01e5d424670bc61ca85b6093a +size 178584 diff --git a/docs/.fonts/Poppins-Thin.ttf b/docs/.fonts/Poppins-Thin.ttf new file mode 100644 index 00000000..26adfe5d --- /dev/null +++ b/docs/.fonts/Poppins-Thin.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:95875f9ef0d12d5cbdd64852933a578021c810cec247f7564207e046cf6c7289 +size 161652 diff --git a/docs/.fonts/Poppins-ThinItalic.ttf b/docs/.fonts/Poppins-ThinItalic.ttf new file mode 100644 index 00000000..f4493967 --- /dev/null +++ b/docs/.fonts/Poppins-ThinItalic.ttf @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:043226b0e187263ab54de3e971b663a77e52c3857cbb235c8410388db6d28de8 +size 187044 diff --git a/docs/.fonts/SIL Open Font License.txt b/docs/.fonts/SIL Open Font License.txt new file mode 100644 index 00000000..d666326d --- /dev/null +++ b/docs/.fonts/SIL Open Font License.txt @@ -0,0 +1,43 @@ +Copyright (c) 2010-2013 by tyPoland Lukasz Dziedzic with Reserved Font Name "Carlito". + +This Font Software is licensed under the SIL Open Font License, Version 1.1. +This license is copied below, and is also available with a FAQ at: http://scripts.sil.org/OFL + +----------------------------------------------------------- +SIL OPEN FONT LICENSE Version 1.1 - 26 February 2007 +----------------------------------------------------------- + +PREAMBLE +The goals of the Open Font License (OFL) are to stimulate worldwide development of collaborative font projects, to support the font creation efforts of academic and linguistic communities, and to provide a free and open framework in which fonts may be shared and improved in partnership with others. + +The OFL allows the licensed fonts to be used, studied, modified and redistributed freely as long as they are not sold by themselves. The fonts, including any derivative works, can be bundled, embedded, redistributed and/or sold with any software provided that any reserved names are not used by derivative works. The fonts and derivatives, however, cannot be released under any other type of license. The requirement for fonts to remain under this license does not apply to any document created using the fonts or their derivatives. + +DEFINITIONS +"Font Software" refers to the set of files released by the Copyright Holder(s) under this license and clearly marked as such. This may include source files, build scripts and documentation. + +"Reserved Font Name" refers to any names specified as such after the copyright statement(s). + +"Original Version" refers to the collection of Font Software components as distributed by the Copyright Holder(s). + +"Modified Version" refers to any derivative made by adding to, deleting, or substituting -- in part or in whole -- any of the components of the Original Version, by changing formats or by porting the Font Software to a new environment. + +"Author" refers to any designer, engineer, programmer, technical writer or other person who contributed to the Font Software. + +PERMISSION & CONDITIONS +Permission is hereby granted, free of charge, to any person obtaining a copy of the Font Software, to use, study, copy, merge, embed, modify, redistribute, and sell modified and unmodified copies of the Font Software, subject to the following conditions: + +1) Neither the Font Software nor any of its individual components, in Original or Modified Versions, may be sold by itself. + +2) Original or Modified Versions of the Font Software may be bundled, redistributed and/or sold with any software, provided that each copy contains the above copyright notice and this license. These can be included either as stand-alone text files, human-readable headers or in the appropriate machine-readable metadata fields within text or binary files as long as those fields can be easily viewed by the user. + +3) No Modified Version of the Font Software may use the Reserved Font Name(s) unless explicit written permission is granted by the corresponding Copyright Holder. This restriction only applies to the primary font name as presented to the users. + +4) The name(s) of the Copyright Holder(s) or the Author(s) of the Font Software shall not be used to promote, endorse or advertise any Modified Version, except to acknowledge the contribution(s) of the Copyright Holder(s) and the Author(s) or with their explicit written permission. + +5) The Font Software, modified or unmodified, in part or in whole, must be distributed entirely under this license, and must not be distributed under any other license. The requirement for fonts to remain under this license does not apply to any document created using the Font Software. + +TERMINATION +This license becomes null and void if any of the above conditions are not met. + +DISCLAIMER +THE FONT SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED TO ANY WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT OF COPYRIGHT, PATENT, TRADEMARK, OR OTHER RIGHT. IN NO EVENT SHALL THE COPYRIGHT HOLDER BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, INCLUDING ANY GENERAL, SPECIAL, INDIRECT, INCIDENTAL, OR CONSEQUENTIAL DAMAGES, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF THE USE OR INABILITY TO USE THE FONT SOFTWARE OR FROM OTHER DEALINGS IN THE FONT SOFTWARE. \ No newline at end of file diff --git a/docs/conf.py b/docs/conf.py index ea094f75..a6dd5d05 100644 --- a/docs/conf.py +++ b/docs/conf.py @@ -14,18 +14,18 @@ # import os import sys -import shutil # Add python modules to be documented python_root = '..' -python_modules = ( 'geos-xml-tools', 'geos-mesh', 'geos-ats', 'hdf5-wrapper', 'pygeos-tools', 'geos-timehistory' ) +python_modules = ( 'geos-ats', 'geos-mesh', 'geos-posp', 'geos-timehistory', 'geos-xml-tools', 'hdf5-wrapper', + 'pygeos-tools' ) for m in python_modules: sys.path.insert( 0, os.path.abspath( os.path.join( python_root, m, 'src' ) ) ) # -- Project information ----------------------------------------------------- project = u'GEOS Python Packages' -copyright = u'2018-2021 Lawrence Livermore National Security, The Board of Trustees of the Leland Stanford Junior University, TotalEnergies, and GEOSX Contributors.' +copyright = u'2018-2024 Lawrence Livermore National Security, The Board of Trustees of the Leland Stanford Junior University, TotalEnergies, and GEOSX Contributors.' author = u'GEOS Contributors' # The short X.Y version @@ -42,12 +42,16 @@ # Add any Sphinx extension module names here, as strings. They can be # extensions coming with Sphinx (named 'sphinx.ext.*') or your custom # ones. -extensions = [ - 'sphinx_design', 'sphinx.ext.todo', 'sphinx.ext.autodoc', 'sphinx.ext.doctest', 'sphinx.ext.imgmath', - 'sphinxarg.ext', 'sphinx.ext.napoleon', 'sphinxcontrib.programoutput' -] +extensions = [ 'sphinx_design', 'sphinx_rtd_theme', 'sphinxarg.ext', 'sphinxcontrib.programoutput', + 'sphinx.ext.autodoc', 'sphinx.ext.doctest', 'sphinx.ext.mathjax', 'sphinx.ext.napoleon', + 'sphinx.ext.todo', 'sphinx.ext.viewcode' ] -autodoc_mock_imports = [ "pygeosx", "pylvarray", "meshio", "lxml", "mpi4py", "h5py", "ats", "scipy" ] +autoclass_content = 'both' +autodoc_mock_imports = [ "ats", "h5py", "lxml", "paraview", "pygeosx", "pylvarray", "meshio", "mpi4py", "scipy" ] +autodoc_typehints = 'none' +autodoc_typehints_format = 'short' +suppress_warnings = [""] +typehints_defaults = 'braces' # The suffix(es) of source filenames. # You can specify multiple suffix as a list of string: @@ -75,21 +79,19 @@ # The name of the Pygments (syntax highlighting) style to use. pygments_style = 'sphinx' -# -- Theme options ---------------------------------------------- -extensions += [ - 'sphinx_rtd_theme', -] - +html_css_files = [ 'theme_overrides.css' ] html_theme = "sphinx_rtd_theme" - html_theme_options = { 'navigation_depth': -1, 'collapse_navigation': False } - +html_sidebars = { + "**": [ + "about.html", + "navigation.html", + "relations.html", # needs 'show_related': True theme option to display + "searchbox.html", + ] +} html_static_path = [ './_static' ] -html_css_files = [ - 'theme_overrides.css', -] - # -- Options for HTMLHelp output --------------------------------------------- # Output file base name for HTML help builder. htmlhelp_basename = 'geosPythonPackagesDoc' diff --git a/docs/geos-posp.rst b/docs/geos-posp.rst new file mode 100644 index 00000000..076b76e5 --- /dev/null +++ b/docs/geos-posp.rst @@ -0,0 +1,12 @@ +GEOS Post-Processing tools +============================= + +.. toctree:: + :maxdepth: 5 + :caption: Contents: + + ./posp_rst/home.rst + + ./posp_rst/modules.rst + + ./posp_rst/visualization.rst diff --git a/docs/images/AttributeMapping.JPG b/docs/images/AttributeMapping.JPG new file mode 100644 index 00000000..c1276a02 --- /dev/null +++ b/docs/images/AttributeMapping.JPG @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:b5890611052d9b7d4eeb76be3e078055850b0a781de8c2fbe86af45b2a85466a +size 131108 diff --git a/docs/images/CreateConstantAttributePerRegionFilter.JPG b/docs/images/CreateConstantAttributePerRegionFilter.JPG new file mode 100644 index 00000000..49ec58e5 --- /dev/null +++ b/docs/images/CreateConstantAttributePerRegionFilter.JPG @@ -0,0 +1,3 @@ +version https://git-lfs.github.com/spec/v1 +oid sha256:4d60f54b6fdf52d9bc68d56b606d153c0c37d129eea31992dbc641390641ca95 +size 136498 diff --git a/docs/images/ExtractMergeBlockFilter.JPG b/docs/images/ExtractMergeBlockFilter.JPG new file mode 100644 index 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sha256:3bb5d122c1f79f61e0ee8f8d05c5638732979dd1dd124647d7bb35a7deb5d802 +size 100937 diff --git a/docs/index.rst b/docs/index.rst index 4a56ec79..a5e7598d 100644 --- a/docs/index.rst +++ b/docs/index.rst @@ -74,7 +74,7 @@ Packages .. toctree:: - :maxdepth: 1 + :maxdepth: 5 hdf5-wrapper @@ -82,8 +82,10 @@ Packages geos-mesh + geos-posp + + geos-timehistory + geos-xml-tools pygeos-tools - - geos-timehistory diff --git a/docs/posp_rst/PVplugins.rst b/docs/posp_rst/PVplugins.rst new file mode 100644 index 00000000..57687c6a --- /dev/null +++ b/docs/posp_rst/PVplugins.rst @@ -0,0 +1,131 @@ +Paraview plugins +================ + +Paraview plugins were developed using Python 3.9.13 and are compatible with Paraview v5.12.0. + +The plugins include: + +* A reader that parse GEOS output log file; +* 3D mesh cleanning plugins; +* Processing plugins to compute additional geomechanical properties; +* Visualization plugins to plot Mohr's circles and cross plots using Paraview Python View. + +PVplugins.PVAttributeMapping module +----------------------------------- + +.. automodule:: PVplugins.PVAttributeMapping + :members: + :undoc-members: + +PVplugins.PVCreateConstantAttributePerRegion module +--------------------------------------------------- + +.. automodule:: PVplugins.PVCreateConstantAttributePerRegion + :members: + :undoc-members: + +PVplugins.PVExtractMergeBlocksVolume module +------------------------------------------- + +.. automodule:: PVplugins.PVExtractMergeBlocksVolume + :members: + :undoc-members: + +PVplugins.PVExtractMergeBlocksVolumeSurface module +-------------------------------------------------- + +.. automodule:: PVplugins.PVExtractMergeBlocksVolumeSurface + :members: + :undoc-members: + +PVplugins.PVExtractMergeBlocksVolumeSurfaceWell module +------------------------------------------------------ + +.. automodule:: PVplugins.PVExtractMergeBlocksVolumeSurfaceWell + :members: + :undoc-members: + +PVplugins.PVExtractMergeBlocksVolumeWell module +----------------------------------------------- + +.. automodule:: PVplugins.PVExtractMergeBlocksVolumeWell + :members: + :undoc-members: + +PVplugins.PVGeomechanicsAnalysis module +--------------------------------------- + +.. automodule:: PVplugins.PVGeomechanicsAnalysis + :members: + :undoc-members: + +PVplugins.PVGeomechanicsWorkflowVolume module +--------------------------------------------- + +.. automodule:: PVplugins.PVGeomechanicsWorkflowVolume + :members: + :undoc-members: + +PVplugins.PVGeomechanicsWorkflowVolumeSurface module +---------------------------------------------------- + +.. automodule:: PVplugins.PVGeomechanicsWorkflowVolumeSurface + :members: + :undoc-members: + +PVplugins.PVGeomechanicsWorkflowVolumeSurfaceWell module +-------------------------------------------------------- + +.. automodule:: PVplugins.PVGeomechanicsWorkflowVolumeSurfaceWell + :members: + :undoc-members: + +PVplugins.PVGeomechanicsWorkflowVolumeWell module +------------------------------------------------- + +.. automodule:: PVplugins.PVGeomechanicsWorkflowVolumeWell + :members: + :undoc-members: + +PVplugins.PVGeosLogReader module +-------------------------------- + +.. automodule:: PVplugins.PVGeosLogReader + :members: + :undoc-members: + +PVplugins.PVMergeBlocksEnhanced module +-------------------------------------- + +.. automodule:: PVplugins.PVMergeBlocksEnhanced + :members: + :undoc-members: + +PVplugins.PVMohrCirclePlot module +--------------------------------- + +.. automodule:: PVplugins.PVMohrCirclePlot + :members: + :undoc-members: + +PVplugins.PVPythonViewConfigurator module +----------------------------------------- + +.. automodule:: PVplugins.PVPythonViewConfigurator + :members: + :undoc-members: + +PVplugins.PVSurfaceGeomechanics module +-------------------------------------- + +.. automodule:: PVplugins.PVSurfaceGeomechanics + :members: + :undoc-members: + +PVplugins.PVTransferAttributesVolumeSurface module +-------------------------------------------------- + +.. automodule:: PVplugins.PVTransferAttributesVolumeSurface + :members: + :undoc-members: + diff --git a/docs/posp_rst/filters.rst b/docs/posp_rst/filters.rst new file mode 100644 index 00000000..da4b0e55 --- /dev/null +++ b/docs/posp_rst/filters.rst @@ -0,0 +1,68 @@ +vtk Filters +=========== + +This package defines vtk filters that allows to process Geos outputs. + +geos_posp.filters.AttributeMappingFromCellCoords module +-------------------------------------------------------- + +.. automodule:: geos_posp.filters.AttributeMappingFromCellCoords + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.AttributeMappingFromCellId module +----------------------------------------------------------- + +.. automodule:: geos_posp.filters.AttributeMappingFromCellId + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.GeomechanicsCalculator module +--------------------------------------------------- + +.. automodule:: geos_posp.filters.GeomechanicsCalculator + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.GeosBlockExtractor module +----------------------------------------------- + +.. automodule:: geos_posp.filters.GeosBlockExtractor + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.GeosBlockMerge module +------------------------------------------- + +.. automodule:: geos_posp.filters.GeosBlockMerge + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.SurfaceGeomechanics module +------------------------------------------------ + +.. automodule:: geos_posp.filters.SurfaceGeomechanics + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.TransferAttributesVolumeSurface module +------------------------------------------------------------ + +.. automodule:: geos_posp.filters.TransferAttributesVolumeSurface + :members: + :undoc-members: + :show-inheritance: + +geos_posp.filters.VolumeSurfaceMeshMapper module +---------------------------------------------------- + +.. automodule:: geos_posp.filters.VolumeSurfaceMeshMapper + :members: + :undoc-members: + :show-inheritance: \ No newline at end of file diff --git a/docs/posp_rst/home.rst b/docs/posp_rst/home.rst new file mode 100644 index 00000000..3ddeed4f --- /dev/null +++ b/docs/posp_rst/home.rst @@ -0,0 +1,44 @@ +Home +==== + +**Geos-posp** is a Python library to read, process and visualize GEOS simulation software outputs. + +**GEOS** is an open-source THM (Thermo-Hydro-Mechanical) simulation framework designed for modeling coupled flow, transport, +and geomechanics in the subsurface on high performance computing platforms. It provides advanced solvers for various applications, +including carbon sequestration and geothermal energy systems. + +Developed as part of the FC-MAELSTROM research project by Lawrence Livermore National Laboratory (LLNL), Stanford University, TotalEnergies, and Chevron, +GEOS draws on their expertise in simulation and high-performance computing research. If you are interested, +you can explore more about GEOS in the `official documentation `_. + +GEOS outputs include: + +* a log file where many simulation statistics are dump into; +* csv and hdf5 files containing simulation properties through time +* a 3D mesh with properties that evolve through time. + +This library is based on `vtk `_ framework and `Paraview `_ visualization software. +It includes: + +* a reader able to parse the GEOS output log to collect data and display them as tables; +* tools to clean imported 3D mesh; +* tools to compute additional geomechanical properties; +* tools to display Mohr's circles at a given time step and the evolution through time. + +The tools included in this library can be used either through: + +* Python scripts that call vtk readers and filters. +* Paraview software by loading plugins located in the PVplugins folder. + + +The current code has been developed on Python 3.9.13 (i.e., Python version used by Paraview 5.12.0) using the following libraries: + +* matplotlib 3.2.1 +* pandas 2.0.1 +* numpy 1.24.3 +* vtk 9.3.2 +* typing_extensions 4.12 + +Additional dependencies: + +* paraview - if plugins are used through Paraview diff --git a/docs/posp_rst/modules.rst b/docs/posp_rst/modules.rst new file mode 100644 index 00000000..889843d5 --- /dev/null +++ b/docs/posp_rst/modules.rst @@ -0,0 +1,15 @@ +Processing +========== + +.. toctree:: + :maxdepth: 5 + + filters + + readers + + processing + + pyvistaTools + + utils diff --git a/docs/posp_rst/processing.rst b/docs/posp_rst/processing.rst new file mode 100644 index 00000000..65d6e83d --- /dev/null +++ b/docs/posp_rst/processing.rst @@ -0,0 +1,69 @@ +Processing functions +==================== + +This package define functions to process data. + + +geos_posp.processing.ConnectionSet module +--------------------------------------------- + +.. automodule:: geos_posp.processing.ConnectionSet + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.geomechanicsCalculatorFunctions module +--------------------------------------------------------------- + +.. automodule:: geos_posp.processing.geomechanicsCalculatorFunctions + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.geometryFunctions module +------------------------------------------------- + +.. automodule:: geos_posp.processing.geometryFunctions + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.geosLogReaderFunctions module +------------------------------------------------------ + +.. automodule:: geos_posp.processing.geosLogReaderFunctions + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.MohrCircle module +------------------------------------------ + +.. automodule:: geos_posp.processing.MohrCircle + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.MohrCoulomb module +------------------------------------------- + +.. automodule:: geos_posp.processing.MohrCoulomb + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.multiblockInpectorTreeFunctions module +--------------------------------------------------------------- + +.. automodule:: geos_posp.processing.multiblockInpectorTreeFunctions + :members: + :undoc-members: + :show-inheritance: + +geos_posp.processing.vtkUtils module +---------------------------------------- + +.. automodule:: geos_posp.processing.vtkUtils + :members: + :undoc-members: + :show-inheritance: diff --git a/docs/posp_rst/pyvistaTools.rst b/docs/posp_rst/pyvistaTools.rst new file mode 100644 index 00000000..d9a4a40f --- /dev/null +++ b/docs/posp_rst/pyvistaTools.rst @@ -0,0 +1,13 @@ +pyvistaTools +============ + +This packages defines utilities using pyvista. + + +geos_posp.pyvistaTools.pyvistaUtils module +----------------------------------------------- + +.. automodule:: geos_posp.pyvistaTools.pyvistaUtils + :members: + :undoc-members: + :show-inheritance: \ No newline at end of file diff --git a/docs/posp_rst/readers.rst b/docs/posp_rst/readers.rst new file mode 100644 index 00000000..588a5910 --- /dev/null +++ b/docs/posp_rst/readers.rst @@ -0,0 +1,36 @@ +vtk Readers +=========== + +This package defines vtk readers that allows to load Geos output files. + +geos_posp.readers.GeosLogReaderAquifers module +-------------------------------------------------- + +.. automodule:: geos_posp.readers.GeosLogReaderAquifers + :members: + :undoc-members: + :show-inheritance: + +geos_posp.readers.GeosLogReaderConvergence module +----------------------------------------------------- + +.. automodule:: geos_posp.readers.GeosLogReaderConvergence + :members: + :undoc-members: + :show-inheritance: + +geos_posp.readers.GeosLogReaderFlow module +---------------------------------------------- + +.. automodule:: geos_posp.readers.GeosLogReaderFlow + :members: + :undoc-members: + :show-inheritance: + +geos_posp.readers.GeosLogReaderWells module +----------------------------------------------- + +.. automodule:: geos_posp.readers.GeosLogReaderWells + :members: + :undoc-members: + :show-inheritance: diff --git a/docs/posp_rst/utils.rst b/docs/posp_rst/utils.rst new file mode 100644 index 00000000..c46c6891 --- /dev/null +++ b/docs/posp_rst/utils.rst @@ -0,0 +1,55 @@ +Utils +===== + +This packages defines utilities including logger, constants, and unit management tools. + + + +geos_posp.utils.GeosOutputsConstants module +------------------------------------------- + +.. automodule:: geos_posp.utils.GeosOutputsConstants + :members: + :undoc-members: + :show-inheritance: + +geos_posp.utils.geosUtils module +--------------------------------- + +.. automodule:: geos_posp.utils.geosUtils + :members: + :undoc-members: + :show-inheritance: + +geos_posp.utils.Logger module +------------------------------ + +.. automodule:: geos_posp.utils.Logger + :members: + :undoc-members: + :show-inheritance: + +geos_posp.utils.PhysicalConstants module +----------------------------------------- + +.. automodule:: geos_posp.utils.PhysicalConstants + :members: + :undoc-members: + :show-inheritance: + +geos_posp.utils.UnitRepository module +------------------------------------- + +.. automodule:: geos_posp.utils.UnitRepository + :members: + :undoc-members: + :show-inheritance: + + +geos_posp.utils.enumUnits module +-------------------------------- + +.. automodule:: geos_posp.utils.enumUnits + :members: + :undoc-members: + :show-inheritance: diff --git a/docs/posp_rst/visu.PVUtils.rst b/docs/posp_rst/visu.PVUtils.rst new file mode 100644 index 00000000..6603a216 --- /dev/null +++ b/docs/posp_rst/visu.PVUtils.rst @@ -0,0 +1,37 @@ +PVUtils Package +=============== + +This packages consists of utilities for Paraview. + + +geos_posp.visu.PVUtils.DisplayOrganizationParaview module +------------------------------------------------------------ + +.. automodule:: geos_posp.visu.PVUtils.DisplayOrganizationParaview + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.PVUtils.checkboxFunction module +------------------------------------------------- + +.. automodule:: geos_posp.visu.PVUtils.checkboxFunction + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.PVUtils.paraviewTreatments module +--------------------------------------------------- + +.. automodule:: geos_posp.visu.PVUtils.paraviewTreatments + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.PVUtils.matplotlibOptions module +---------------------------------------------------------- + +.. automodule:: geos_posp.visu.PVUtils.matplotlibOptions + :members: + :undoc-members: + :show-inheritance: \ No newline at end of file diff --git a/docs/posp_rst/visu.mohrCircles.rst b/docs/posp_rst/visu.mohrCircles.rst new file mode 100644 index 00000000..988e4c4c --- /dev/null +++ b/docs/posp_rst/visu.mohrCircles.rst @@ -0,0 +1,28 @@ +Mohr's Circle Package +===================== + +This package includes utilities to compute and plot Mohr's Circles using the Python View from Paraview. + +geos_posp.visu.mohrCircles.functionsMohrCircle module +-------------------------------------------------------- + +.. automodule:: geos_posp.visu.mohrCircles.functionsMohrCircle + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.mohrCircles.mainMohrCircles module +---------------------------------------------------- + +.. automodule:: geos_posp.visu.mohrCircles.mainMohrCircles + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.mohrCircles.plotMohrCircles module +-------------------------------------------------- + +.. automodule:: geos_posp.visu.mohrCircles.plotMohrCircles + :members: + :undoc-members: + :show-inheritance: diff --git a/docs/posp_rst/visu.pythonViewUtils.rst b/docs/posp_rst/visu.pythonViewUtils.rst new file mode 100644 index 00000000..0442aae6 --- /dev/null +++ b/docs/posp_rst/visu.pythonViewUtils.rst @@ -0,0 +1,31 @@ +PythonViewUtils Package +============================ + +This package includes utilities to display cross-plot using the Python View from Paraview. + + +geos_posp.visu.pythonViewUtils.Figure2DGenerator module +---------------------------------------------------------- + +.. automodule:: geos_posp.visu.pythonViewUtils.Figure2DGenerator + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.pythonViewUtils.functionsFigure2DGenerator module +------------------------------------------------------------------- + +.. automodule:: geos_posp.visu.pythonViewUtils.functionsFigure2DGenerator + :members: + :undoc-members: + :show-inheritance: + +geos_posp.visu.pythonViewUtils.mainPythonView module +------------------------------------------------------- + +.. automodule:: geos_posp.visu.pythonViewUtils.mainPythonView + :members: + :undoc-members: + :show-inheritance: + + diff --git a/docs/posp_rst/visu.rst b/docs/posp_rst/visu.rst new file mode 100644 index 00000000..c6e782b7 --- /dev/null +++ b/docs/posp_rst/visu.rst @@ -0,0 +1,14 @@ +Utilities +========= + +This package includes visualization tools dedicated to Paraview software. + + +.. toctree:: + :maxdepth: 4 + + visu.PVUtils + + visu.mohrCircles + + visu.pythonViewUtils \ No newline at end of file diff --git a/docs/posp_rst/visualization.rst b/docs/posp_rst/visualization.rst new file mode 100644 index 00000000..f63db3ec --- /dev/null +++ b/docs/posp_rst/visualization.rst @@ -0,0 +1,9 @@ +Visualization +============= + +.. toctree:: + :maxdepth: 4 + + PVplugins + + visu \ No newline at end of file diff --git a/docs/requirements.txt b/docs/requirements.txt index 6ecdf80c..19ab47d3 100644 --- a/docs/requirements.txt +++ b/docs/requirements.txt @@ -1,6 +1,8 @@ +pandas sphinx >= 7.4.7 sphinx_rtd_theme sphinx-argparse >= 0.5.2 +sphinx-autodoc-typehints sphinx-design # Running CLI programs and capture outputs sphinxcontrib-programoutput>=0.17 diff --git a/docs/user_guide.md b/docs/user_guide.md new file mode 100644 index 00000000..67d60441 --- /dev/null +++ b/docs/user_guide.md @@ -0,0 +1,628 @@ +--- +Title: GEOS Paraview Plugins User Guide +SubTitle: PV plugins to process GEOS inputs/outputs +Author: Martin LEMAY +Company: TotalEnergies +Date: January 29, 2025 +--- + + +
+ + +{{ Title }} + + + +{{ SubTitle }} + + +{{ Author }} + +*{{ CurrentDate }}* + +















+ +
+ +
+ + + +## Outline + +- [1. Introduction](#1-introduction) + - [1.1. Paraview at a glance](#11-paraview-at-a-glance) + - [1.2. Paraview filters for GEOS](#12-paraview-filters-for-geos) +- [2. Pre-processing GEOS inputs](#2-pre-processing-geos-inputs) +- [3. Load and plot GEOS Log Data](#3-load-and-plot-geos-log-data) + - [3.1. GEOS Log Reader](#31-geos-log-reader) + - [3.2. Plot data from spreadsheets using Python View Configurator](#32-plot-data-from-spreadsheets-using-python-view-configurator) +- [4. Load and clean GEOS output mesh and properties](#4-load-and-clean-geos-output-mesh-and-properties) +- [5. Geomechanics Post-Processing](#5-geomechanics-post-processing) + - [5.1. Compute additional geomechanical properties](#51-compute-additional-geomechanical-properties) + - [5.2. Compute additional surfacic geomechanical properties](#52-compute-additional-surfacic-geomechanical-properties) + - [5.3. Geomechanics workflows](#53-geomechanics-workflows) + - [5.4. Plot 2D Mohr's Circles for geomechanics studies](#54-plot-2d-mohrs-circles-for-geomechanics-studies) +- [6. Utilities](#6-utilities) + - [6.1. Transfer attributes between identical or partial meshes](#61-transfer-attributes-between-identical-or-partial-meshes) + - [6.2. Transfer properties from Volume mesh to surfaces](#62-transfer-properties-from-volume-mesh-to-surfaces) + - [6.3. Merge blocks keeping partial attributes](#63-merge-blocks-keeping-partial-attributes) +- [7. Other tools around GEOS](#7-other-tools-around-geos) + - [7.1. GEOS Python tools](#71-geos-python-tools) + - [7.2. geos-xml-viewer](#72-geos-xml-viewer) + +
+ +## What you will learn in this documentation + +* What are GEOS outputs: +* How to load and plot information from GEOS output log +* How to load and process GEOS output mesh +* How to compute additional geomechanical outputs +* How to plot Mohr's circles +* How to create scatter plots + + +## Prerequisites + +**On GEOS** + +* Get the output mesh with properties in pvd format +* Get the simulation log in .txt or .out format + +**On Paraview** + +* Basic knowledge of Paraview + +
+ +# 1. Introduction + +## 1.1. Paraview at a glance + +Paraview (PV) is an open source application and architecture for the 2D and 3D visualization and analysis of large scale scientific data sets. It has been developed by the Kitware company since 2000 and is merely funded by DOE programs or by external companies. It is downloaded approximately 100,000 times a year and is recognized as a leader scientific visualization application by many institutions and companies. It has initially been designed for computational fluid dynamics visualizations but its extensible and modular architecture enables it to extend to new areas. It makes ParaView a general purpose tool for a wide range of applications. + +For more details, see the following documentation: +* [Paraview website and user guides](https://docs.paraview.org/en/latest/index.html) + +
+ +## 1.2. Paraview filters for GEOS + +GEOS is a R&D simulation software, which implies that: + +* input data must be cautiously prepared to be compliant with GEOS +* output data must be post-processed to be visualized or to be compliant with other softwares + +To this end, several tools have been developed around GEOS to pre-process and post-process GEOS inputs/outputs (see section [Other tools around GEOS](#7-other-tools-around-geos)) and to integrate it in the global geomedeling workflow. + +
+ +In particular, several Paraview plugins have been developed to enable the users to visualize data -especially unstructured meshes- and to make the tools more user-friendly. These plugins and described in the following. + +Filters are organized as following in the `Filters` menu: +* `0- Geos Pre-Processing`: filters to process the mesh before GEOS simulations +* `1- Geos Post-Processing Workflows`: Composite filters that combine individual post-processing filters to apply on GEOS simulation results. +* `2- Geos Output Mesh Pre-Processing`: Individual post-processing filters to apply on GEOS simulation results to clean the mesh. +* `3- Geos Geomechanics`: Individual filters to perform geomechanic analysis of GEOS simulation results. +* `4- Geos Utils`: Individual filters to process and visualize the mesh. + +
+ +![GEOS filters](images/GEOS_filter_organisation.JPG) + +
Figure 1: GEOS filter organization in Paraview.
+
+
+ +# 2. Pre-processing GEOS inputs + +GEOS input data needs to be processed from the geomedeller to make it valid for GEOS. Most of these operations are currently made by [`mesh-doctor`](#71-geos-python-tools) and [`geos-xml-viewer`](#72-geos-xml-viewer), and Paraview plugins are not available yet for these tools. + +The pre-processing `Create Constant attribute Per Region` filter was however developed in Paraview to ease the creation of properties constant per regions, such region being defined using another index property. +Input mesh can be of any type and composite. The user needs to select the region property, to define the name of output property, and to defined the values of the output property for each region index. If no value is defined for some region indexes, the output property will yield no data value in these regions. + +> [!IMPORTANT] +> #### To use this filter +> +> 1. Select the mesh you want to add an attribute +> 2. Apply `Create Constant attribute Per Region` filter +> 3. Define input parameters +> 4. Click on `Apply` + +In the example shown in the Figure hereafter, the mesh consists of 3 regions defined using the property named "region" whose values are (0, 1, 2) and can be seen in the 3D viewer on the left hand. A new property named here "Porosity" is created whose values are: + +* 0.05 in region index 0 +* 0.15 in region index 1 +* 0.2 in region index 2 + +The resulting property is shown in the 3D viewer on the right hand. + +
+ +![GEOS filters](images/CreateConstantAttributePerRegionFilter.JPG) + +
Figure 2: "CreateConstantAttributePerRegion" filter.
+ +
+
+ + +# 3. Load and plot GEOS Log Data + +GEOS dumps data in a log file whose name is usually "job_GEOS_[JOB ID].out". This text file can be read by the user. It contains: +* the list of all the events that happens during the simulation + + +
+ +![GEOS log file](images/GEOS_log_start.JPG) + +
Figure 3: GEOS output log file - GEOS events.
+ +
+
+ +* if activated, a lot of information on: + * Flow properties + * Well properties + * Aquifer properties + * Solver properties + +
+ +![GEOS log - time step data](images/GEOS_log_time_step.JPG) + +
Figure 6: GEOS output log file - Time step information.
+ +
+
+ +This log file is currently the subject of a lot of work by the GEOS Integration Team to make the information clearer and more easily readible. + +The data contained in this file can also be loaded in Paraview as a spreadsheet to be processed and plotted. + +> [!TIP] +> #### How to export simulation data to GEOS log in GEOS xml file? +> +> Information dumped into the log file is controlled by the field `log_level` from `Statistics` tasks in the xml file. +> +>
+> +> GEOS xml - flow solvers +> +> GEOS xml - wells +> +>
Figure 4: Activation of statistic outputs in the GEOS xml file.
+>
+ +## 3.1. GEOS Log Reader + +A Paraview plugin has been developped to read GEOS log file. To load a log file, the user uses the `Open` command from Paraview, selects the log file, then selects the right reader named `Geos Log Reader`. + +
+ +GEOS Log Reader + +
Figure 5: Steps to open GEOS log file using "GEOS Log Reader".
+ +
+
+ +The user can now select in the `Properties` panel the information type to load among: + +* `Flow` properties statistics +* `Wells` properties statistics +* `Aquifers` properties +* `Convergence` metrics + +All the properties read in the file are listed and can be manually selected. In addition, the user can enter the phase names if they are known, and choose working units. + +
+ +![GEOS Log Reader - Properties Panel](images/GEOS_log_Reader1.JPG) + +
Figure 6: "GEOS log Reader" - Properties panel.
+ +
+
+ +Loaded data are displayed in a SpreadSheetView. + +
+ +![GEOS Log Data](images/GEOS_log_data_spreadsheet.JPG) + +
Figure 7: Loaded properties as a spreadsheet using "GEOS log Reader".
+ +
+
+ +> [!TIP] +> If the user wants to load multiple property types from the log (e.g., both Flow and Wells), the same file must be loaded twice using GEOS Log Reader and selecting in each one the correct type. + +> [!CAUTION] +> The reader is compliant until the GEOS commit version #9365098. +> +> Use the **csv export** options for more recent versions of GEOS and directly load the csv into Paraview. + +> [!TIP] +> #### How to export simulation data to csv file in GEOS xml file? +> +> Information dumped into the csv file is controlled by the field `writecsv` from `Statistics` tasks in the xml file. +> +>
+> +> GEOS xml - csv export +> +>
Figure 8: Activation of csv export in the GEOS xml file.
+>
+ +## 3.2. Plot data from spreadsheets using Python View Configurator + +A common task is to plot the data loaded from GEOS log file or csv files. To do that, a plugin has been developped to create and display plots in Paraview using the `PythonView`. + +The user must choose the filter `Filters>4- Geos Utils>Python View Configurator`. In the `Properties` panel, the following parameters must be defined: + +* Input sources: input data source to plot +* Curves To Plot: abcissa and ordinate data to plot. Multiple curve can be plotted in the same graph, but a same scale is used for all of them. If some regions are defined, data can be splitted by regions if the checkbox is toggled. +* Curve Convention: Toggle to select from the list the curves to change convention (multiplied by -1). This is usefull for instance to plot Stress and Pressure on a same plot using the right convention. +* Axis Properties: Toggle `Edit Axis Properties` to access to axis properties. Axes can be reversed, use a log scale, display minor ticks, or set limits. +* Title Properties: Toggle `Display Title` to add a title to the figure and edit font properties. +* Legend Properties: Toggle `Display Legend` to add a legend to the figure and edit position and labels. +* Curves Properties: Toggle `Edit Curve Graphics` to edit markers and line properties. + +> [!IMPORTANT] +> #### To use this filter +> 1. Select input data to plot +> 2. Apply `Python View Configurator` filter +> 3. Define input parameters +> 4. Click on `Apply` + +
+ +![Pressure vs Time](images/pressure_vs_time.JPG) + +
Figure 9: Plot Pressure vs. Time using "Python View Configurator" filter from GEOS log outputs.
+ +
+
+ +> [!TIP] +> `Python View Configurator` is able to plot data from any spreadsheets, whatever its origin (e.g., data along a line). +> The image hereafter shows an example of pipeline and `Python View Configurator` filter parameters to plot Pressure, total and effective stresses against the depth. +> +>
+> +> ![Pressure and Stress vs Depth](images/stress_along_well.JPG) +> +>
Figure 10: Steps to Plot Pressure and Stress vs. Depth using "Python View Configurator" filter from GEOS output mesh.
+> +>
+ +# 4. Load and clean GEOS output mesh and properties + +GEOS may result in an output mesh containing simulated properties at multiple time steps. The export format is a `.pvd` xml file referring to the corresponding vtm file for each time step. + +
+ +GEOS output pvd file + +
Figure 11: pvd file containing time step value and path to corresponding vtm file.
+ +
+
+ +> [!TIP] +> #### How to activate vtk output mesh in GEOS xml file? +> +> To activate the output mesh, xml file must contains the following sections: +> * `` with the `VTK` field, where `fieldNames` allows to define exported properties, and set `logLevel` key to 2. +> * `` with `` pointing to vtk output name. +> +>
+> +> ![GEOS output mesh](images/GEOS_XML_vtkOutput.JPG) +> +>
Figure 12: Activation of output mesh in GEOS XML file.
+> +>
+ +To load GEOS output mesh in Paraview, the user uses the `Open` command from Paraview and selects the `.pvd` file. The file name must appears in the Pipeline Browser. The user may display the properties in the 3D View, and run through the time steps using the `Time Manager` toolbar. + +> [!TIP] +> The `.pvd` file can be copied and manually edited to select desired time steps to save computation time in Paraview. + +GEOS output mesh is a composite data set containing all the objects used in the simulation including the volume mesh, surfaces (faults), and wells. Each object may contain regions -e.g., one region per layer in the volume mesh, one region per fault, or one region per well- and each region is splitted in ranks because of parallel processing during GEOS simulation. In addition, property names take the name of the region they are computed. Consequently a property may have various prefix although it represents a same property -e.g., "reservoir_Porosity", "overburden_Porosity", "underburden_Porosity". + +
+ +MultiBlock inspector + +
Figure 13: Paraview MultiBlock Inspector showing GEOS output mesh architecture.
+ +
+
+ +A set of 4 filters located in `Filters>2 Geos Output Mesh Pre-Processing` can be used to clean the mesh depending on mesh content: `Geos Extract And Merge Blocks - Volume Only`, `Geos Extract And Merge Blocks - Volume/Surface`, `Geos Extract And Merge Blocks - Volume/Surface/Well`, `Geos Extract And Merge Blocks - Volume/Well`. These filters result in one, two, or three outputs, `output-0` being the volume mesh, `output-1` being surfaces or wells if 2 outputs are present, `output-3` being wells. +These filters do the following operations: +* merge rank blocks for each regions and create "blockIndex" property to keep memory of ranks +* merge properties whose names contain various prefix and rename some properties like "stress" in "effectiveStress" +* copy some property values from initial time step to the other time steps ("Porosity", "effectiveStress", "Pressure") +* compute surface normal and tangent vectors + +> [!IMPORTANT] +> #### To use this filter +> 1. Select GEOS output mesh +> 2. Apply one of `Geos Extract And Merge Blocks` filters according to the data content +> 3. Click on `Apply` + +
+ +![GeosExtractAndMergeBlocks](images/ExtractMergeBlockFilter.JPG) + +
Figure 14: "Geos Extract And Merge Blocks" filters.
+ +
+
+ +# 5. Geomechanics Post-Processing + +GEOS computes many outputs including flow and geomechanic properties if coupled flow geomechanics simulations were run. Users however need additional metrics to asses geomechanical stability as part of operational studies. Two filters have been developped to compute these additional metrics: `Geos Geomechanics Analysis` and `Geos Surfacic Geomechanics`. In addition, a third filter allows to plot Mohr's circles on selected cells and time steps. + +## 5.1. Compute additional geomechanical properties + +`Geos Geomechanics Analysis` filter located in `Filters>3 Geos Geomechanics` computes additional geomechanics properties on input object (volume, surface, polyline mesh). +This filter has the following input parameters: +* grain bulk modulus to compute Biot coefficient if the property is not in the mesh +* the reference density used to compute specific gravity +* if `Compute Advanced Geomechanical Outputs` is toggled, other metrics are computed. Additional parameters are rock cohesion (in Pa) and friction angle (in °). + +> [!IMPORTANT] +> #### To use this filter +> 1. Select output-0 from one of `Geos Extract And Merge Blocks` filters +> 2. Apply `Geos Geomechanics Analysis` filter +> 3. Define input parameters +> 4. Click on `Apply` + +
+ +![Geomechanics Analysis filter](images/GeomechanicsAnalysis.JPG) + +
Figure 15: "GEOS Geomechanics Analysis" filter applied on a volume mesh.
+ +
+
+ +All properties are computed if they are not already present in the mesh as a GEOS output. + +
Table 1: Geomechanical basic outputs.
+ +|
Property
|
Property Name
|
Formulae
| +| ------------------- | ------------------- | --------------------------- | +| Young modulus | youngModulus | $E=\frac{9K.G}{3K+G}$ | +| Poisson ratio | poissonRatio | $\nu=\frac{3K-2G}{2(3K+G)}$ | +| Bulk modulus | bulkModulus | $K=\frac{E}{3(1-2\nu)}$ | +| Shear modulus | shearModulus | $G=\frac{E}{2(1+\nu)}$ | +| Biot coefficient | biotCoefficient | $b=1-\frac{K}{K_{grain}}$ | +| Specific gravity | specificGravity | $SG=\frac{\rho}{\rho_{ref}}$ | +| Elastic strain | strainElastic | $\epsilon=\Delta\sigma_{eff}.C^{-1}$ | +| Effective stress ratio
in oedometric conditions | stressEffectiveRatio_oed | $r_{eff}^{oed}=\frac{\nu}{1-\nu}$ | +| Effective stress ratio
in real conditions | stressEffectiveRatio_real | $r_{eff}^{real}=\frac{\sigma_{eff}^h}{\sigma_{eff}^v}$ | | +| Total stress | stressTotal | $\sigma_{tot}=\sigma_{eff}-bP$ | | +| Total stress deviation | deltaStressTotal | $\Delta\sigma_{tot}=\sigma_{tot}^{@t}-\sigma_{tot}^{@t_0}$ | +| Total stress ratio
in real conditions | stressTotalRatio_real | $r_{tot}=\frac{\sigma_{tot}^h}{\sigma_{tot}^v}$ | +| Reservoir Stress Path
in oedometric conditions | RSP_oed | $RSP_{oed}=b\frac{1-2\nu}{1-\nu}$ | +| Reservoir Stress Path
in real conditions | RSP_real | $RSP_{real}=\frac{\Delta\sigma}{\Delta P}$ | +| Compressibility coefficient
in oedometric conditions | compressibility_oed | $C_{oed}=\frac{1}{\phi}.\frac{3}{3K+4G}$ | +| Compressibility coefficient
in real conditions | compressibility_real | $C_{real}=\frac{\phi-\phi_0}{\Delta P.\phi_0}$ | + +where $\rho$ is density, $\rho_{ref} is reference density, $K_{grain}$ is grain bulk modulus, $\sigma_{eff}$ is effective stress, *P* is pressure, exponent *h* and *v* stand for horizontal and vertical (e.g., $\sigma_{eff}^v$ is vertical effective stress), *C* is stiffness tensor, $\Delta$ stands for deviation from initial time step (e.g., $\Delta P$ is pressure deviation). + +
Table 2: Geomechanical advanced outputs.
+ +|
Property
|
Property Name
|
Formulae
|
Comment
| +| ------------------- | ------------------- | --------------------------- | ------- | +| Critical total stress ratio | totalStressRatioCritical_real | $\sigma_{Ĉr}=\frac{P}{\sigma_v}$ | Corresponds to the fracture index from Lemgruber-Traby et al (2024). Fracturing can occur in areas where K > Total stress ratio. (see [Lemgruber-Traby, A., Cacas, M. C., Bonte, D., Rudkiewicz, J. L., Gout, C., & Cornu, T. (2024). Basin modelling workflow applied to the screening of deep aquifers for potential CO2 storage. Geoenergy, geoenergy2024-010.](https://doi.org/10.1144/geoenergy2024-010)) | +| Total stress ratio threshold | totalStressRatioThreshold_real | $\sigma_{Th}=\frac{P}{\sigma_h}$ | Corresponds to the fracture threshold from Lemgruber-Traby et al (2024). Fracturing can occur in areas where FT > 1. Equals FractureIndex / totalStressRatio. (see [Lemgruber-Traby, A., Cacas, M. C., Bonte, D., Rudkiewicz, J. L., Gout, C., & Cornu, T. (2024). Basin modelling workflow applied to the screening of deep aquifers for potential CO2 storage. Geoenergy, geoenergy2024-010.](https://doi.org/10.1144/geoenergy2024-010)) | +| Critical pore pressure | porePressureCritical_real | $P_{Cr}=\frac{c.\cos(\alpha)}{1-\sin(\alpha)} + \frac{3\sigma_3-\sigma_1}{2}$ | Fracturing can occur in areas where Critical pore pressure is greater than the pressure. (see [Khan, S., Khulief, Y., Juanes, R., Bashmal, S., Usman, M., & Al-Shuhail, A. (2024). Geomechanical Modeling of CO2 Sequestration: A Review Focused on CO2 Injection and Monitoring. Journal of Environmental Chemical Engineering, 112847.](https://doi.org/10.1016/j.jece.2024.112847)) | +| Pore pressure threshold | porePressureThreshold_real | $P_{Th}=\frac{P}{P_{Cr}}$ | Defined as the ratio between pressure and critical pore pressure. Fracturing can occur in areas where critical pore pressure threshold is >1. (see [Khan, S., Khulief, Y., Juanes, R., Bashmal, S., Usman, M., & Al-Shuhail, A. (2024). Geomechanical Modeling of CO2 Sequestration: A Review Focused on CO2 Injection and Monitoring. Journal of Environmental Chemical Engineering, 112847.](https://doi.org/10.1016/j.jece.2024.112847)) | + +where *c* is rock cohesion and $\alpha$ is friction angle. + +> [!CAUTION] +> Elastic moduli properties -i.e., either Shear and Bulk moduli, or Young modulus and Poisson ratio- are necessary to compute additional geomechanical properties. An error message warns the user if these properties are missing. + + +> #### How to output elastic moduli in GEOS xml file? +> +> Elastic moduli properties can be manually added to the output mesh in Paraview using for instance the `Calculator` filter. But if these moduli vary in space and/or time, it is better to export the properties in the output mesh. +> +> To do that, the `fieldNames` key from `VTK` field in the `` section of GEOS xml file must contains the list of output property names like `rock_bulkModulus`, `rock_shearModulus`, `rock_youngModulus`, `rock_poissonRatio`, etc. (e.g., ![GEOS output mesh]), where `rock` refers to `materialList` key elements from `ElementRegions` field in the xml file. + +> [!CAUTION] +> This filter must be applied to output-0 from `Geos Extract And Merge Blocks` filters. + +## 5.2. Compute additional surfacic geomechanical properties + +`Geos Surfacic Geomechanics` filter located in `Filters>3 Geos Geomechanics` computes additional geomechanics properties and is dedicated to surfaces. This filter computes: +* the displacementJump property in the XYZ axes in addition to normal and tangential axes given by GEOS. +* the shear capacity utilization (SCU) property. This calculation needs rock cohesion (in Pa) and friction angle (in °) to compute failure threshold. SCU formula is: $SCU = \frac{abs(\tau_1)}{\tau_{max}}$, where $\tau_1$ is the maximal principal stress and $\tau_{max}$ is the failure threshold. + +> [!IMPORTANT] +> #### To use this filter +> 1. Select output-1 from `Geos Extract And Merge Blocks - Volume/Surface` or `Geos Extract And Merge Blocks - Volume/Surface/Well` filters +> 2. Apply one of `Geos Surfacic Geomechanics` filter +> 3. Define input parameters +> 4. Click on `Apply` + +
+ +![Surface Geomechanics](images/SurfaceGeomechanics.JPG) + +
Figure 16: "GEOS Surface Geomechanics" filter.
+ +
+
+ +> [!IMPORTANT] +> This filter must be applied to output-1 from `Geos Extract And Merge Blocks - Volume/Surface` or `Geos Extract And Merge Blocks - Volume/Surface/Well` filters. + +## 5.3. Geomechanics workflows + +During geomechanical studies, users will most often have to apply one of the `Geos Extract And Merge Blocks` filters, then `Geos Geomechanics Analysis` on output-0 and/or `Geos Surface Geomechanics` on output-1. + +`Geos Geomechanics Workflow` filters located in `Filters>1-Geos Post-Processing Workflows` gather the successive application of these filters in a single one depending on input objects. Results are the same as the combination of the elementary filters. + +> [!IMPORTANT] +> #### To use this filter +> 1. Select GEOS output mesh +> 2. Apply one of `Geos Geomechanics Workflow` filters according to the data content +> 3. Define input parameters +> 4. Click on `Apply` + +
+ +![Geomechanics Workflows](images/GeomechanicsWorkflows.JPG) + +
Figure 17: "GEOS Geomechanics Workflow - Volume/Surface" filter.
+ +
+
+ +## 5.4. Plot 2D Mohr's Circles for geomechanics studies + +Geomechanical studies most often rely on Mohr-s circle analysis. Mohr's circle can be plotted from a selection of cells and time steps using `Plot Mohr's Circles` filter located in `Filters>3-Geos Geomechanics`. + +Input parameters in the `Properties` panel are: +* Ids of the cell to plot +* Time steps to plot +* Mohr-Coulomb failure envelop parameters -i.e., rock cohesion (in Pa) and friction angle (in °) +* Stress unit used for axes +* Stress convention (default is positive for compression) +* Annotate circle checkbox allows to show/hide normal stress values +* show/hide minor ticks +* Show/Hide title and Legend parameters like font properties and legend location +* Show/Hide user-defined axis limits definition panel +* Show/Hide curve aspect edition panel + +> [!IMPORTANT] +> #### To use this filter +> 1. Extract a reduce number of cells from GEOS output mesh (`Find Data>Extract Selection`) ([see Paraview documentatin](https://docs.paraview.org/en/latest/UsersGuide/selectingData.html)) +> 2. Apply `MergeBlocks` filter +> 3. Apply `Plot Mohr's Circles` filter +> 4. Select circles to plot +> 5. Select plot parameters +> 6. Click on `Apply` + +
+ +![Mohr's circles plot](images/mohr_circle_plot.JPG) + +
Figure 18: Steps to plot Mohr's circles using "Plot Mohr's Circle" filter from GEOS output mesh.
+ +
+
+ +> [!CAUTION] +> `Plot Mohr's Circles` must be applied on a limited number of cells and input mesh must be merged (even if it consists of a single cell) + +# 6. Utilities + +`Filters>4-Geos Utilities` menu contains generic filters including `Python View Configurator` (see section *[3.2. Plot data from spreadsheets using Python View Configurator](#32-plot-data-from-spreadsheets-using-python-view-configurator))* and `Geos Transfer Attributes From Volume To Surface` filter. + +In addition, writers have also been developped and are accessible using `Save Data` command of Paraview by selecting the appropriate output format. Currently, an exporter of a text file for EST containing map properties from GEOS simulation is available. + +## 6.1. Transfer attributes between identical or partial meshes + +The filter `Attribute Mapping` allows to transfer properties from a server mesh to a client mesh. The server and client meshes must be either strictly identical or one an extract from the other one. The server mesh must be a single block dataset, whereas the output mesh can be a single or multi block dataset. + +> [!IMPORTANT] +> #### To use this filter +> 1. Select the server mesh from which properties will be transferred +> 2. Select the `Attribute Mapping` filter +> 3. In the dialog, check the server mesh then select the client mesh the properties to transfer go to +> 4. In the `Properties` panel, select the properties to transfer +> 5. Click on `Apply` + +> In the following example, the property "region" was transferred from GEOS input mesh (to the left) to GEOS output mesh (to the right). + +
+ +![Transfer properties between 2 meshes](images/AttributeMapping.JPG) + +
Figure 19: Application of "Attribute Mapping" filter.
+ +
+
+ +## 6.2. Transfer properties from Volume mesh to surfaces + +`Geos Transfer Attributes From Volume To Surface` filter allows to transfer attributes initially stored on the volume mesh to a surface mesh. The surface mesh must be conformal to the volume mesh -i.e., surface and volume mesh vertices are collocated and surface faces correspond to volume cell faces. + +Because a surface usually defines a boundary of the model, properties may be discontinuous on both sides of the surface. Two properties are thus created on the surface using the name of input property and a suffix "_minus" and "_plus". Each property corresponds to the property value of cells adjacent to the surface along one side or the other. + +> [!IMPORTANT] +> #### To use this filter +> 1. Select the volume mesh the properties to transfer are from +> 2. Apply `Geos Transfer Attributes From Volume To Surface` filter +> 3. In the dialog, select the surface mesh the properties to transfer go to +> 4. In the `Properties` panel, select the properties to transfer +> 5. Click on `Apply` + +> In the following example, the property "totalStressThreshold_real" was transferred from volume to surface mesh. Top 3D viewer shows the volume mesh with the property and the surface edges in white. +> Bottom left viewer shows the property on the surface ("totalStressThreshold_real_minus") that was transferred from the volume to right side of the surface, bottom right viewer shows the property on the surface ("totalStressThreshold_real_plus") that was transferred from the volume to the left side of the surface. + +
+ +![Transfer attributes from volume to surface mesh](images/TransferAttributes.JPG) + +
Figure 20: Application of "Geos Transfer Attributes From Volume To Surface" filter.
+ +
+
+ +> [!CAUTION] +> `Transfer Attributes From Volume To Surface` filter must be cautiously applied since the results may be nonsense. + +## 6.3. Merge blocks keeping partial attributes + +Paraview provides the `Merge Blocks` filter to merge multiblock mesh to a single block mesh. However, if some properties are partial (i.e., present in some blocks of different data type but not all), they are removed in the output mesh. The filter `Merge Blocks Keeping Partial Attributes` extends the `Merge Blocks` filter by transferring in the output mesh partial properties. They take the *nan* value where the attributes were absent. + +> [!IMPORTANT] +> #### To use this filter +> 1. Select the volume mesh to merge +> 2. Apply `Merge Blocks Keeping Partial Attributes` filter +> 3. Click on `Apply` + +> In the following example, the mesh to the rigth is a multiBlock dataset containing partial attributes including the pressure defined only in the mid unit. After applying `Merge Blocks Keeping Partial Attributes` filter, all the blocks were merged together and all the attributes are present in the merged dataset. + +
+ +![Merge blocks and keep partial attributes](images/MergeBlocksEnhanced.JPG) + +
Figure 21: Application of "Merge Blocks Keeping Partial Attributes" filter.
+ +
+
+ +# 7. Other tools around GEOS + +Other tools allow GEOS users to prepare GEOS input data. Except geos2est for which a Paraview plugin exists, these tools do not have a Paraview interface yet. + +## 7.1. GEOS Python tools + +`GEOS Python tools` allows to process GEOS input and output data (See [documentation](https://geosx-geosx.readthedocs-hosted.com/projects/geosx-geospythonpackages/en/latest/?_sm_au_=iMVrtR60VT6jHPNtQ0WpHK6H8sjL6)). + +Among these tools, [`mesh-doctor`](https://geosx-geosx.readthedocs-hosted.com/projects/geosx-geospythonpackages/en/latest/geos-mesh.html?_sm_au_=iMVrtR60VT6jHPNtQ0WpHK6H8sjL6) processes GEOS input data to make it compliant with GEOS. + +## 7.2. geos-xml-viewer + +`geos-xml-viewer` is a Python package dedicated to visualize and process GEOS input xml file (deck). This package provides the following main functionalities: +* create a PartitionedDataSetCollection from vtu file and objects defined in the GEOS deck +* visualize deck objects (mesh, wells, boxes) +* split a deck into multiple files (e.g. one per main node) + + + \ No newline at end of file diff --git a/geos-posp/.gitignore b/geos-posp/.gitignore new file mode 100644 index 00000000..bcef4e44 --- /dev/null +++ b/geos-posp/.gitignore @@ -0,0 +1,167 @@ +# Byte-compiled / optimized / DLL files +__pycache__/ +*.py[cod] +*$py.class + +# C extensions +*.so + +# Distribution / packaging +.Python +build/ +develop-eggs/ +dist/ +downloads/ +eggs/ +.eggs/ +lib/ +lib64/ +parts/ +sdist/ +var/ +wheels/ +share/python-wheels/ +*.egg-info/ +.installed.cfg +*.egg +MANIFEST + +# PyInstaller +# Usually these files are written by a python script from a template +# before PyInstaller builds the exe, so as to inject date/other infos into it. +*.manifest +*.spec + +# Installer logs +pip-log.txt +pip-delete-this-directory.txt + +# Unit test / coverage reports +htmlcov/ +.tox/ +.nox/ +.coverage +.coverage.* +.cache +nosetests.xml +coverage.xml +*.cover +*.py,cover +.hypothesis/ +.pytest_cache/ +cover/ + +# Translations +*.mo +*.pot + +# Django stuff: +*.log +local_settings.py +db.sqlite3 +db.sqlite3-journal + +# Flask stuff: +instance/ +.webassets-cache + +# Scrapy stuff: +.scrapy + +# Sphinx documentation +docs/_build/ + +# PyBuilder +.pybuilder/ +target/ + +# Jupyter Notebook +.ipynb_checkpoints + +# IPython +profile_default/ +ipython_config.py + +# pyenv +# For a library or package, you might want to ignore these files since the code is +# intended to run in multiple environments; otherwise, check them in: +.python-version + +# pipenv +# According to pypa/pipenv#598, it is recommended to include Pipfile.lock in version control. +# However, in case of collaboration, if having platform-specific dependencies or dependencies +# having no cross-platform support, pipenv may install dependencies that don't work, or not +# install all needed dependencies. +#Pipfile.lock + +# poetry +# Similar to Pipfile.lock, it is generally recommended to include poetry.lock in version control. +# This is especially recommended for binary packages to ensure reproducibility, and is more +# commonly ignored for libraries. +# https://python-poetry.org/docs/basic-usage/#commit-your-poetrylock-file-to-version-control +#poetry.lock + +# pdm +# Similar to Pipfile.lock, it is generally recommended to include pdm.lock in version control. +#pdm.lock +# pdm stores project-wide configurations in .pdm.toml, but it is recommended to not include it +# in version control. +# https://pdm.fming.dev/latest/usage/project/#working-with-version-control +.pdm.toml +.pdm-python +.pdm-build/ + +# PEP 582; used by e.g. github.com/David-OConnor/pyflow and github.com/pdm-project/pdm +__pypackages__/ + +# Celery stuff +celerybeat-schedule +celerybeat.pid + +# SageMath parsed files +*.sage.py + +# Environments +.env +.venv +env/ +venv/ +ENV/ +env.bak/ +venv.bak/ + +# Spyder project settings +.spyderproject +.spyproject + +# Rope project settings +.ropeproject + +# mkdocs documentation +/site + +# mypy +.mypy_cache/ +.dmypy.json +dmypy.json + +# Pyre type checker +.pyre/ + +# pytype static type analyzer +.pytype/ + +# Cython debug symbols +cython_debug/ + +# PyCharm +# JetBrains specific template is maintained in a separate JetBrains.gitignore that can +# be found at https://github.com/github/gitignore/blob/main/Global/JetBrains.gitignore +# and can be added to the global gitignore or merged into this file. For a more nuclear +# option (not recommended) you can uncomment the following to ignore the entire idea folder. +#.idea/ + +# VScode project +*.vscode/*.json +*.vscode-codespaces* +Thumbs.db diff --git a/geos-posp/README.md b/geos-posp/README.md new file mode 100644 index 00000000..0cb307cb --- /dev/null +++ b/geos-posp/README.md @@ -0,0 +1,113 @@ +# + +## Description + +This package provides several python tools to read, process and visualize GEOS simulation software outputs in Paraview. + +GEOS outputs include a log file where many simulation statistics are dump into and a 3D mesh with properties that evolve through time. +A reader allows to parse the log to collect data and display them as tables. Other tools process the 3D mesh to clean data and compute new properties. + +The following content will present the Python plugins. + +## Installation + +The current code has been developed on Python 3.9.13 using the following libraries: +- matplotlib >= 3.2.1 +- pandas >= 2.0.1 +- numpy >= 1.24.3 +- vtk >= 9.3.2 +- paraview >= 5.11.1 +- pyvista >= 0.44 + +The package includes: +- PVplugins: contains all Paraview plugins +- geos-posp: + * filters: contains vtk filters + * readers: contains vtk readers + * writers: contains vtk writers + * processing: contains processing modules used by vtk filters and readers + * utils: contains utilities + * visu: contains Paraview display and plotting functions + * bin: contains applications + +The tools included in this package can be used either through: +- python scripts that call vtk readers and filters. +- Paraview by loading plugins located in the PVplugins folder. + +## Paraview plugins Usage + +The procedure to load Paraview plugins is the following: +1) Open the plugins manager in Tools -> Manage Plugins + All available plugins are listed by their name, and a property "Loaded" or "Not Loaded". + +2) If the wanted plugins are already in the list and loaded, no need to go further, they are ready to be used in Paraview. + +3) If the wanted plugins are already in the list but not loaded, click on each one and apply "Load selected". + Their property should switch to "Loaded" when done. + +4) If the wanted plugins are not in the list, they can be imported by: + Click on "Load New", go to the "PVplugins" folder, then select every needed plugin, and click "OK". + They should normally appear in the list as "Loaded" when done. + +**NOTE**: Plugins can be automatically loaded when lauching ParaView by checking the option "Auto Load" in the drop down menu of the selected plugin in the plugin manager list. + +PVAttributeMapping.py +---------------------- + +PVAttributeMapping is a Paraview Filter that transfer attributes from an input mesh to an output mesh. Both mesh must be either identical or one a subset of the other one. + +PVCreateConstantAttributePerRegion.py +------------------------------------- + +PVCreateConstantAttributePerRegion is a Paravie Filter that allows the user to create new attributes with constant values per regions. These regions are defined from another attribute present in the input mesh. + +PVGeosExtractMergeBlocksVolume*.py +---------------------------------- + +They are a set of 4 Paraview filters (PVGeosExtractMergeBlocksVolume.py, PVGeosExtractMergeBlocksVolumeSurface.py, PVGeosExtractMergeBlocksVolumeWell.py, PVGeosExtractMergeBlocksVolumeSurfaceWell.py) to clean GEOS output mesh, surfaces, and wells depending on the data contained in the .pvd output file from GEOS. + +PVGeomechanicsAnalysis.py +----------------------- + +PVGeomechanicsAnalysis is a Paraview Filter that computes additional geomechanical properties in an output mesh from a poro-mechanical simulation with GEOS. + +PVSurfaceGeomechanics.py +----------------------- + +PVSurfaceGeomechanics is a Paraview Filter that computes additional geomechanical properties specific to surfacic objects in an output mesh from a contact poro-mechanical simulation with GEOS. + +PVGeomechanicsWorkflowVolume*.py +--------------------------------- + +They are a set of 4 Paraview Filters (PVGeomechanicsWorkflowVolume.py, PVGeomechanicsWorkflowVolumeSurface.py, PVGeomechanicsWorkflowVolumeWell.py, PVGeomechanicsWorkflowVolumeSurfaceWell.py) that combines PVGeosExtractMergeBlocksVolume* and geomechanics filters (PVGeomechanicsAnalysis and PVSurfaceGeomechanics) depending on input objects. + +PVMergeBocksEnhanced.py +----------------------- + +PVMergeBocksEnhanced is a Paraview filter that merge blocks of various types and keep partial attributes. + +PVMohrCirclePlot.py +----------------------- + +PVMohrCirclePlot is a Paraview Filter that create a Mohr's circle plot from selected cells at all time steps. + +PVTransferAttributesVolumeSurface.py +------------------------------------ + +PVTransferAttributesVolumeSurface is a Paraview filter that transfer attributes from a volume mesh to a conformal surface mesh. + +PythonViewConfigurator.py +----------------------- + +PythonViewConfigurator is a Paraview Filter that cross-plots selected data in a new Python View layout. + + +PVGeosLogReader.py +----------------------- + +GeosLogReader is a Paraview Reader that load GEOS log files with the extension ".out" or ".txt" as a vtkTable. +A list of options allows to choose which information to extract from the log file. + +## Credits + +This work benefits from inputs from all the SIM/CS team members and GEOS developers and users. diff --git a/geos-posp/package-lock.json b/geos-posp/package-lock.json new file mode 100644 index 00000000..bcdfad3e --- /dev/null +++ b/geos-posp/package-lock.json @@ -0,0 +1,1877 @@ +{ + "name": "slider-template", + "lockfileVersion": 3, + "requires": true, + "packages": { + "": { + "dependencies": { + "decktape": "^3.12.0" + } + }, + "node_modules/decktape": { + "version": "3.12.0", + "resolved": "https://registry.npmjs.org/decktape/-/decktape-3.12.0.tgz", + "integrity": "sha512-yrhOyWkSG9yMsJBgcE0q8tmq1os7ty8rwdedKlDirfGvIB3u+2JrYA0zY5oL4GJbMwPUh9Zy2/NwY3g8ZctUjg==", + "hasShrinkwrap": 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post-process data from the geos simulation tool." +authors = [{name = "Martin Lemay", email = "martin.lemay@external.totalenergies.com"}] +license = {text = "Apache-2.0"} +classifiers = [ + "Intended Audience :: Developers", + "Development Status :: 4 - Beta", + "License :: OSI Approved :: Apache Software License ", + "Natural Language :: English", + "Operating System :: OS Independent", + "Programming Language :: Python :: 3 :: Only", + "Topic :: Scientific/Engineering :: Visualization", +] +keywords = [ + "GEOS", + "Simulation", +] +dependencies = [ + "vtk >= 9.3", + "numpy >= 1.26", + "pandas >= 2.2", + "typing_extensions >= 4.12", +] +requires-python = ">= 3.9" + +[project.urls] +Homepage = "https://github.com/GEOS-DEV/geosPythonPackages" +Documentation = "https://geosx-geosx.readthedocs-hosted.com/projects/geosx-geospythonpackages/en/latest/" +Repository = "https://github.com/GEOS-DEV/geosPythonPackages.git" +"Bug Tracker" = "https://github.com/GEOS-DEV/geosPythonPackages/issues" + +[project.optional-dependencies] +dev = [ + "black", + "ruff", + "mypy", +] +test = [ + "coverage", + "pytest" +] + +[project.readme] +file = "README.md" +content-type = "text/markdown" + +[tool.bumpversion] +current_version = "1.0.0" + +[[tool.bumpversion.files]] +filename = "pyproject.toml" +search = 'version = "{current_version}"' + +[tool.ruff] +target-version = "py39" + +src = ["src"] + +extend-exclude = ["tests/Data"] + +# Same as Black. +line-length = 88 +indent-width = 4 + +[tool.ruff.lint] +select = [ + "E", # pycodestyle errors + "W", # pycodestyle warnings + "F", # pyflakes +# "UP", # pyupgrade deactivate since python39 + "B", # flake8-bugbear + "SIM", # flake8-simplify + "ANN", # flake8-annotations + "C4", # flake8-comprehensions + "I", # isort + "D", # pydocstyle +] + +ignore = [ + "E501", # line too long, handled by black + "B008", # do not perform function calls in argument defaults + "C901", # too complex + "W191", # indentation contains tabs + "D100", + "D101", + "D104", # Missing docstring in public package in __init__.py files + "UP007", +] + +# Allow fix for all enabled rules (when `--fix`) is provided. +fixable = ["ALL"] +unfixable = [] + +# Allow unused variables when underscore-prefixed. +dummy-variable-rgx = "^(_+|(_+[a-zA-Z0-9_]*[a-zA-Z0-9]+?))$" + +[tool.ruff.lint.isort] +known-third-party = ["pyvista"] + +#[tool.ruff.lint.pyupgrade] +# Preserve types, even if a file imports `from __future__ import annotations`. +#keep-runtime-typing = true + +[tool.ruff.lint.pydocstyle] +convention = "google" + +[tool.ruff.format] +# Like Black, use double quotes for strings. +quote-style = "double" + +# Like Black, indent with spaces, rather than tabs. +indent-style = "space" + +# Like Black, automatically detect the appropriate line ending. +line-ending = "auto" + +[tool.pytest.ini_options] +addopts = [ + "--import-mode=importlib", +] +console_output_style = "count" +python_classes = "Test" +python_files = "tests*.py" +python_functions = "test*" +testpaths = ["tests"] +pythonpath = [ + "src", +] + +[tool.coverage.run] +branch = true +source = ["PVplugins", "geos-posp"] + +[tool.mypy] +# Specify the target platform details in config, so your developers are +# free to run mypy on Windows, Linux, or macOS and get consistent +# results. +python_version = "3.9" +files = "." +exclude = "build/*" +# strict = true + +warn_unreachable = true +implicit_reexport = true +show_error_codes = true +show_column_numbers = true +disable_error_code = "misc" + +# Overrides for currently untyped modules +[[tool.mypy.overrides]] +module = [ + "docs.*", + "docs.ext.*", + "tests.unit.*", +] +ignore_errors = true diff --git a/geos-posp/shell.nix b/geos-posp/shell.nix new file mode 100644 index 00000000..1d1dae35 --- /dev/null +++ b/geos-posp/shell.nix @@ -0,0 +1,14 @@ +{ pkgs ? import {} }: + +with pkgs; + +mkShell { +buildInputs = [ +nodejs-18_x pandoc +]; +shellHook = '' + npm install + export PATH="$PWD/node_modules/.bin/:$PATH" + ''; + +} diff --git a/geos-posp/src/PVplugins/PVAttributeMapping.py b/geos-posp/src/PVplugins/PVAttributeMapping.py new file mode 100644 index 00000000..c8387acf --- /dev/null +++ b/geos-posp/src/PVplugins/PVAttributeMapping.py @@ -0,0 +1,303 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Raphaël Vinour, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +from typing_extensions import Self, Union + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtkmodules.vtkCommonCore import ( + vtkDataArraySelection, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCompositeDataSet, + vtkDataObjectTreeIterator, + vtkDataSet, + vtkMultiBlockDataSet, + vtkUnstructuredGrid, +) + +from geos_posp.filters.AttributeMappingFromCellCoords import ( + AttributeMappingFromCellCoords, +) +from geos_posp.processing.vtkUtils import ( + fillPartialAttributes, + getAttributeSet, + getNumberOfComponents, + mergeBlocks, +) +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.visu.PVUtils.checkboxFunction import ( # type: ignore[attr-defined] + createModifiedCallback, +) +from geos_posp.visu.PVUtils.paraviewTreatments import getArrayChoices + +__doc__ = """ +Map the attributes from a source mesh to a client mesh. + +Input and output are vtkUnstructuredGrid. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVAttributeMapping. +* Select the server mesh. +* Search and Select Attribute Mapping Filter. +* Select the client mesh. +* Select the attributes to transfer and Apply. + +""" + + +@smproxy.filter(name="PVAttributeMapping", label="Attribute Mapping") +@smhint.xml('') +@smproperty.input(name="Client", port_index=1, label="Client mesh") +@smdomain.datatype( + dataTypes=["vtkUnstructuredGrid", "vtkMultiBlockDataSet"], + composite_data_supported=True, +) +@smproperty.input(name="Server", port_index=0, label="Server mesh") +@smdomain.datatype( + dataTypes=["vtkUnstructuredGrid"], + composite_data_supported=False, +) +class PVAttributeMapping(VTKPythonAlgorithmBase): + + def __init__(self: Self) -> None: + """Map the properties of a server mesh to a client mesh.""" + super().__init__( + nInputPorts=2, nOutputPorts=1, outputType="vtkUnstructuredGrid" + ) + + # boolean to check if first use of the filter for attribute list initialization + self.m_firstUse = True + + # list of attribute names to transfer + self.m_attributes: vtkDataArraySelection = vtkDataArraySelection() + self.m_attributes.AddObserver(0, createModifiedCallback(self)) + + # logger + self.m_logger: Logger = getLogger("Attribute Mapping") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + self.Modified() + + @smproperty.dataarrayselection(name="AttributesToTransfer") + def a02GetAttributeToTransfer(self: Self) -> vtkDataArraySelection: + """Get selected attribute names to transfer. + + Returns: + vtkDataArraySelection: selected attribute names. + """ + return self.m_attributes + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + # only at initialization step, no change later + if self.m_firstUse: + # get cell ids + inData = self.GetInputData(inInfoVec, 0, 0) + assert isinstance( + inData, (vtkDataSet, vtkMultiBlockDataSet) + ), "Input object type is not supported." + + # update vtkDAS + attributeNames: set[str] = getAttributeSet(inData, False) + for attributeName in attributeNames: + if not self.m_attributes.ArrayExists(attributeName): + self.m_attributes.AddArray(attributeName) + + self.m_firstUse = False + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 1, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + + self.m_logger.info(f"Apply filter {__name__}") + try: + serverMesh: Union[ + vtkUnstructuredGrid, vtkMultiBlockDataSet, vtkCompositeDataSet + ] = self.GetInputData(inInfoVec, 0, 0) + clientMesh: Union[ + vtkUnstructuredGrid, vtkMultiBlockDataSet, vtkCompositeDataSet + ] = self.GetInputData(inInfoVec, 1, 0) + outData: Union[ + vtkUnstructuredGrid, vtkMultiBlockDataSet, vtkCompositeDataSet + ] = self.GetOutputData(outInfoVec, 0) + + assert serverMesh is not None, "Input server mesh is null." + assert clientMesh is not None, "Input client mesh is null." + assert outData is not None, "Output pipeline is null." + + outData.ShallowCopy(clientMesh) + attributeNames: set[str] = set( + getArrayChoices(self.a02GetAttributeToTransfer()) + ) + for attributeName in attributeNames: + nbComponents = getNumberOfComponents(serverMesh, attributeName, False) + fillPartialAttributes(serverMesh, attributeName, nbComponents, False) + + mergedServerMesh: vtkUnstructuredGrid + if isinstance(serverMesh, vtkUnstructuredGrid): + mergedServerMesh = serverMesh + elif isinstance(serverMesh, (vtkMultiBlockDataSet, vtkCompositeDataSet)): + mergedServerMesh = mergeBlocks(serverMesh) + else: + raise ValueError( + "Server mesh data type is not supported. " + + "Use either vtkUnstructuredGrid or vtkMultiBlockDataSet" + ) + + if isinstance(outData, vtkUnstructuredGrid): + self.doTransferAttributes(mergedServerMesh, outData, attributeNames) + elif isinstance(outData, (vtkMultiBlockDataSet, vtkCompositeDataSet)): + self.transferAttributesMultiBlockDataSet( + mergedServerMesh, outData, attributeNames + ) + else: + raise ValueError( + "Client mesh data type is not supported. " + + "Use either vtkUnstructuredGrid or vtkMultiBlockDataSet" + ) + + outData.Modified() + mess: str = f"Attributes were successfully transferred ." + self.m_logger.info(mess) + except AssertionError as e: + mess1: str = "Attribute transfer failed due to:" + self.m_logger.error(mess1) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Attribute transfer failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def doTransferAttributes( + self: Self, + serverMesh: vtkUnstructuredGrid, + clientMesh: vtkUnstructuredGrid, + attributeNames: set[str], + ) -> bool: + """Transfer attributes between two vtkUnstructuredGrids. + + Args: + serverMesh (vtkUnstructuredGrid): server mesh + clientMesh (vtkUnstructuredGrid): client mesh + attributeNames (set[str]): set of attribut names to transfer + + Returns: + bool: True if attributes were successfully transferred. + + """ + filter: AttributeMappingFromCellCoords = AttributeMappingFromCellCoords() + filter.AddInputDataObject(0, serverMesh) + filter.AddInputDataObject(1, clientMesh) + filter.SetTransferAttributeNames(attributeNames) + filter.Update() + clientMesh.ShallowCopy(filter.GetOutputDataObject(0)) + return True + + def transferAttributesMultiBlockDataSet( + self: Self, + serverBlock: vtkUnstructuredGrid, + clientMesh: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], + attributeNames: set[str], + ) -> bool: + """Transfer attributes from a vtkUnstructuredGrid to a multiblock. + + Args: + serverBlock (vtkUnstructuredGrid): server mesh + clientMesh (vtkMultiBlockDataSet | vtkCompositeDataSet): client mesh + attributeNames (set[str]): set of attribut names to transfer + + Returns: + bool: True if attributes were successfully transferred. + + """ + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(clientMesh) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + clientBlock: vtkUnstructuredGrid = vtkUnstructuredGrid.SafeDownCast( + iter.GetCurrentDataObject() + ) + self.doTransferAttributes(serverBlock, clientBlock, attributeNames) + clientBlock.Modified() + iter.GoToNextItem() + return True diff --git a/geos-posp/src/PVplugins/PVCreateConstantAttributePerRegion.py b/geos-posp/src/PVplugins/PVCreateConstantAttributePerRegion.py new file mode 100644 index 00000000..2f948b91 --- /dev/null +++ b/geos-posp/src/PVplugins/PVCreateConstantAttributePerRegion.py @@ -0,0 +1,326 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +from typing import Union + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import vtkmodules.util.numpy_support as vnp +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtk import VTK_DOUBLE # type: ignore[import-untyped] +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkDataObject, + vtkMultiBlockDataSet, + vtkUnstructuredGrid, +) + +from geos_posp.processing.multiblockInpectorTreeFunctions import ( + getBlockElementIndexesFlatten, + getBlockFromFlatIndex, +) +from geos_posp.processing.vtkUtils import isAttributeInObject +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +PVCreateConstantAttributePerRegion is a Paraview plugin that allows to +create 2 attributes whom values are constant for each region index. + +Input and output are either vtkMultiBlockDataSet or vtkUnstructuredGrid. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVCreateConstantAttributePerRegion. +* Select the mesh you want to create the attributes and containing a region attribute. +* Search and Apply Create Constant Attribute Per Region Filter. + +""" + +SOURCE_NAME: str = "" +DEFAULT_REGION_ATTRIBUTE_NAME = "region" + + +@smproxy.filter( + name="PVCreateConstantAttributePerRegion", + label="Create Constant Attribute Per Region", +) +@smhint.xml("""""") +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype( + dataTypes=["vtkMultiBlockDataSet", "vtkUnstructuredGrid"], + composite_data_supported=True, +) +class PVCreateConstantAttributePerRegion(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Create an attribute with constant value per region.""" + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkDataSet") + + self.m_table: list[tuple[int, float]] = [] + self.m_regionAttributeName: str = DEFAULT_REGION_ATTRIBUTE_NAME + self.m_attributeName: str = "attribute" + + # logger + self.m_logger: Logger = getLogger("Create Constant Attribute Per Region Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + @smproperty.xml( + """ + + + + + + + + Select an attribute containing the indexes of the regions + + + """ + ) + def a01SetRegionAttributeName(self: Self, name: str) -> None: + """Set region attribute name.""" + self.m_regionAttributeName = name + self.Modified() + + @smproperty.xml( + """ + + + Name of the new attribute + + + """ + ) + def a02SetAttributeName(self: Self, value: str) -> None: + """Set attribute name. + + Args: + value (str): attribute name. + """ + self.m_attributeName = value + self.Modified() + + @smproperty.xml( + """ + + + + + + + + + Set new attributes values for each region index. + + + """ + ) + def b01SetAttributeValues(self: Self, regionIndex: int, value: float) -> None: + """Set attribute values per region. + + Args: + regionIndex (int): region index. + + value (float): attribute value. + """ + self.m_table.append((regionIndex, value)) + self.Modified() + + @smproperty.xml( + """ + + """ + ) + def b02GroupFlow(self: Self) -> None: + """Organize groups.""" + self.Modified() + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, # noqa: F841 + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + self.m_logger.info(f"Apply filter {__name__}") + try: + input0: Union[vtkUnstructuredGrid, vtkMultiBlockDataSet] = ( + self.GetInputData(inInfoVec, 0, 0) + ) + output: Union[vtkUnstructuredGrid, vtkMultiBlockDataSet] = ( + self.GetOutputData(outInfoVec, 0) + ) + + assert input0 is not None, "Input Surface is null." + assert output is not None, "Output pipeline is null." + + output.ShallowCopy(input0) + + assert ( + len(self.m_regionAttributeName) > 0 + ), "Region attribute is undefined, please select an attribute." + if isinstance(output, vtkMultiBlockDataSet): + self.createAttributesMultiBlock(output) + else: + self.createAttributes(output) + + mess: str = ( + f"The new attribute {self.m_attributeName} was successfully added." + ) + self.Modified() + self.m_logger.info(mess) + except AssertionError as e: + mess1: str = "The new attribute was not added due to:" + self.m_logger.error(mess1) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "The new attribute was not added due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + self.m_compute = True + return 1 + + def createAttributesMultiBlock(self: Self, output: vtkMultiBlockDataSet) -> None: + """Create attributes on vtkMultiBlockDataSet from input data. + + Args: + output (vtkMultiBlockDataSet): mesh where to create the attributes. + """ + # for each block + blockIndexes: list[int] = getBlockElementIndexesFlatten(output) + for blockIndex in blockIndexes: + block0: vtkDataObject = getBlockFromFlatIndex(output, blockIndex) + assert block0 is not None, "Block is undefined." + block: vtkUnstructuredGrid = vtkUnstructuredGrid.SafeDownCast(block0) + try: + self.createAttributes(block) + except AssertionError as e: + self.m_logger.warning(f"Block {blockIndex}: {e}") + output.Modified() + + def createAttributes(self: Self, mesh: vtkUnstructuredGrid) -> None: + """Create attributes on vtkUnstructuredGrid from input data. + + Args: + + mesh (vtkUnstructuredGrid): mesh where to create the attributes. + """ + assert isAttributeInObject( + mesh, self.m_regionAttributeName, False + ), f"{self.m_regionAttributeName} is not in the mesh." + regionAttr: vtkDataArray = mesh.GetCellData().GetArray( + self.m_regionAttributeName + ) + assert regionAttr is not None, "Region attribute is undefined" + npArray: npt.NDArray[np.float64] = self.createNpArray(regionAttr) + newAttr: vtkDataArray = vnp.numpy_to_vtk(npArray, True, VTK_DOUBLE) + newAttr.SetName(self.m_attributeName) + mesh.GetCellData().AddArray(newAttr) + mesh.GetCellData().Modified() + mesh.Modified() + + def createNpArray(self: Self, regionAttr: vtkDataArray) -> npt.NDArray[np.float64]: + """Create numpy arrays from input data. + + Args: + regionAttr (vtkDataArray): Region attribute + + Returns: + npt.NDArray[np.float64]: numpy array of the new attribute. + """ + regionNpArray: npt.NDArray[np.float64] = vnp.vtk_to_numpy(regionAttr) + npArray: npt.NDArray[np.float64] = np.full_like(regionNpArray, np.nan) + # for each region + for regionIndex, value in self.m_table: + if regionIndex in np.unique(regionNpArray): + mask: npt.NDArray[np.bool_] = regionNpArray == regionIndex + npArray[mask] = value + else: + self.m_logger.warning( + f"Index {regionIndex} is not in the values of the region" + + f" attribute '{regionAttr.GetName()}'" + ) + return npArray diff --git a/geos-posp/src/PVplugins/PVExtractMergeBlocksVolume.py b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolume.py new file mode 100644 index 00000000..15d06021 --- /dev/null +++ b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolume.py @@ -0,0 +1,331 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkMultiBlockDataSet + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.filters.GeosBlockExtractor import GeosBlockExtractor +from geos_posp.filters.GeosBlockMerge import GeosBlockMerge +from geos_posp.processing.vtkUtils import ( + copyAttribute, + createCellCenterAttribute, +) +from geos_posp.utils.GeosOutputsConstants import ( + GeosMeshOutputsEnum, + getAttributeToTransferFromInitialTime, +) +from geos_posp.utils.Logger import ERROR, INFO, Logger, getLogger +from geos_posp.visu.PVUtils.paraviewTreatments import getTimeStepIndex + +__doc__ = """ +PVExtractMergeBlocksVolume is a Paraview plugin that allows to merge ranks +of a Geos output objects containing only a volumic mesh. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in a single output pipeline that contains the volume mesh. +If multiple regions were defined in the volume mesh, they are preserved as +distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVExtractMergeBlocksVolume. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVExtractMergeBlocksVolume Filter. + +""" + + +@smproxy.filter( + name="PVExtractMergeBlocksVolume", + label="Geos Extract And Merge Blocks - Volume Only", +) +@smhint.xml( + """ + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVExtractMergeBlocksVolume(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to extract and merge ranks from Geos output Mesh. + + To apply in the case of output ".pvd" file contains only a Volume. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=1, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: all time steps from input + self.m_timeSteps: npt.NDArray[np.float64] = np.array([]) + #: displayed time step in the IHM + self.m_currentTime: float = 0.0 + #: time step index of displayed time step + self.m_currentTimeStepIndex: int = 0 + #: request data processing step - incremented each time RequestUpdateExtent is called + self.m_requestDataStep: int = -1 + + #: saved object at initial time step + self.m_outputT0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + + #: set logger + self.m_logger: Logger = getLogger("Extract and merge block Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestUpdateExtent( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestUpdateExtent. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() + inInfo = inInfoVec[0] + # get displayed time step info before updating time + if self.m_requestDataStep == -1: + self.m_logger.info(f"Apply filter {__name__}") + self.m_timeSteps = inInfo.GetInformationObject(0).Get( + executive.TIME_STEPS() # type: ignore + ) + self.m_currentTime = inInfo.GetInformationObject(0).Get( + executive.UPDATE_TIME_STEP() # type: ignore + ) + self.m_currentTimeStepIndex = getTimeStepIndex( + self.m_currentTime, self.m_timeSteps + ) + # update requestDataStep + self.m_requestDataStep += 1 + + # update time according to requestDataStep iterator + inInfo.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), self.m_timeSteps[self.m_requestDataStep] # type: ignore + ) + outInfoVec.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), self.m_timeSteps[self.m_requestDataStep] # type: ignore + ) + + # update all objects according to new time info + self.Modified() + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + output: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 0) + + assert input is not None, "Input object is null." + assert output is not None, "Output object is null." + + # time controller + executive = self.GetExecutive() + if self.m_requestDataStep == 0: + # first time step + # do extraction and merge (do not display phase info) + self.m_logger.setLevel(ERROR) + self.doExtractAndMerge(input, output) + self.m_logger.setLevel(INFO) + # save input mesh to copy later + self.m_outputT0.ShallowCopy(output) + request.Set(executive.CONTINUE_EXECUTING(), 1) # type: ignore + if self.m_requestDataStep >= self.m_currentTimeStepIndex: + # displayed time step, no need to go further + request.Remove(executive.CONTINUE_EXECUTING()) # type: ignore + # reinitialize requestDataStep if filter is recalled later + self.m_requestDataStep = -1 + # do extraction and merge + self.doExtractAndMerge(input, output) + # copy attributes from initial time step + for ( + attributeName, + attributeNewName, + ) in getAttributeToTransferFromInitialTime().items(): + copyAttribute( + self.m_outputT0, output, attributeName, attributeNewName + ) + # create elementCenter attribute if needed + cellCenterAttributeName: str = ( + GeosMeshOutputsEnum.ELEMENT_CENTER.attributeName + ) + createCellCenterAttribute(output, cellCenterAttributeName) + + # TODO add ForceStaticMesh filter https://gitlab.kitware.com/paraview/plugins/staticmeshplugin + + except AssertionError as e: + mess: str = "Block extraction and merge failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Block extraction and merge failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + + return 1 + + def doExtractAndMerge( + self: Self, input: vtkMultiBlockDataSet, output: vtkMultiBlockDataSet + ) -> bool: + """Apply block extraction and merge. + + Args: + input (vtkMultiBlockDataSet): input multi block + output (vtkMultiBlockDataSet): output volume mesh + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + # extract blocks + blockExtractor: GeosBlockExtractor = GeosBlockExtractor() + blockExtractor.SetLogger(self.m_logger) + blockExtractor.SetInputDataObject(input) + blockExtractor.Update() + + # recover output objects from GeosBlockExtractor filter + volumeBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputVolume() + assert volumeBlockExtracted is not None, "Extracted Volume mesh is null." + + # merge internal blocks + output.ShallowCopy(self.mergeBlocksFilter(volumeBlockExtracted, False)) + output.Modified() + self.m_logger.info("Ranks were successfully merged together.") + return True + + def mergeBlocksFilter( + self: Self, input: vtkMultiBlockDataSet, convertSurfaces: bool = False + ) -> vtkMultiBlockDataSet: + """Apply vtk merge block filter on input multi block mesh. + + Args: + input (vtkMultiBlockDataSet): multiblock mesh to merge + convertSurfaces (bool, optional): True to convert surface from vtkUnstructuredGrid to + vtkPolyData. Defaults to False. + + Returns: + vtkMultiBlockDataSet: Multiblock mesh composed of internal merged blocks. + """ + mergeBlockFilter: GeosBlockMerge = GeosBlockMerge() + mergeBlockFilter.SetLogger(self.m_logger) + mergeBlockFilter.SetInputDataObject(input) + if convertSurfaces: + mergeBlockFilter.ConvertSurfaceMeshOn() + else: + mergeBlockFilter.ConvertSurfaceMeshOff() + mergeBlockFilter.Update() + mergedBlocks: vtkMultiBlockDataSet = mergeBlockFilter.GetOutputDataObject(0) + assert mergedBlocks is not None, "Final merged MultiBlockDataSet is null." + return mergedBlocks diff --git a/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeSurface.py b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeSurface.py new file mode 100644 index 00000000..efb0d2c0 --- /dev/null +++ b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeSurface.py @@ -0,0 +1,361 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkMultiBlockDataSet + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.filters.GeosBlockExtractor import GeosBlockExtractor +from geos_posp.filters.GeosBlockMerge import GeosBlockMerge +from geos_posp.processing.vtkUtils import ( + copyAttribute, + createCellCenterAttribute, +) +from geos_posp.utils.GeosOutputsConstants import ( + GeosMeshOutputsEnum, + getAttributeToTransferFromInitialTime, +) +from geos_posp.utils.Logger import ERROR, INFO, Logger, getLogger +from geos_posp.visu.PVUtils.paraviewTreatments import getTimeStepIndex + +__doc__ = """ +PVExtractMergeBlocksVolumeSurface is a Paraview plugin that allows to merge +ranks of a Geos output objects containing a volumic mesh and surfaces. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in 2 output pipelines: + +* first pipeline contains the volume mesh. If multiple regions were defined in + the volume mesh, they are preserved as distinct blocks. +* second pipeline contains surfaces. If multiple surfaces were used, they are + preserved as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVExtractMergeBlocksVolumeSurface. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVExtractMergeBlocksVolumeSurface Filter. + +""" + + +@smproxy.filter( + name="PVExtractMergeBlocksVolumeSurface", + label="Geos Extract And Merge Blocks - Volume/Surface", +) +@smhint.xml( + """ + + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVExtractMergeBlocksVolumeSurface(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to extract and merge ranks from Geos output Mesh. + + To apply in the case of output ".pvd" file contains Volume and Fault + elements. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=2, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: all time steps from input + self.m_timeSteps: npt.NDArray[np.float64] = np.array([]) + #: displayed time step in the IHM + self.m_currentTime: float = 0.0 + #: time step index of displayed time step + self.m_currentTimeStepIndex: int = 0 + #: request data processing step - incremented each time RequestUpdateExtent is called + self.m_requestDataStep: int = -1 + + # saved object at initial time step + self.m_outputT0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + + # set logger + self.m_logger: Logger = getLogger("Extract and merge block Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outDataCells = self.GetOutputData(outInfoVec, 0) + outDataFaults = self.GetOutputData(outInfoVec, 1) + assert inData is not None + if outDataCells is None or (not outDataCells.IsA("vtkMultiBlockDataSet")): + outDataCells = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(0).Set( + outDataCells.DATA_OBJECT(), outDataCells + ) # type: ignore + if outDataFaults is None or (not outDataFaults.IsA("vtkMultiBlockDataSet")): + outDataFaults = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(1).Set( + outDataFaults.DATA_OBJECT(), outDataFaults + ) # type: ignore + + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestUpdateExtent( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestUpdateExtent. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() + inInfo = inInfoVec[0] + # get displayed time step info before updating time + if self.m_requestDataStep == -1: + self.m_logger.info(f"Apply filter {__name__}") + self.m_timeSteps = inInfo.GetInformationObject(0).Get( + executive.TIME_STEPS() + ) # type: ignore + self.m_currentTime = inInfo.GetInformationObject(0).Get( + executive.UPDATE_TIME_STEP() + ) # type: ignore + self.m_currentTimeStepIndex = getTimeStepIndex( + self.m_currentTime, self.m_timeSteps + ) + # update requestDataStep + self.m_requestDataStep += 1 + + # update time according to requestDataStep iterator + inInfo.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), # type: ignore + self.m_timeSteps[self.m_requestDataStep], + ) + outInfoVec.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), # type: ignore + self.m_timeSteps[self.m_requestDataStep], + ) + + # update all objects according to new time info + self.Modified() + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + outputCells: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 0) + outputFaults: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 1) + + assert input is not None, "Input MultiBlockDataSet is null." + assert outputCells is not None, "Output volum mesh is null." + assert outputFaults is not None, "Output surface mesh is null." + + # time controller + executive = self.GetExecutive() + if self.m_requestDataStep == 0: + # first time step + # do extraction and merge (do not display phase info) + outputFaults0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + self.m_logger.setLevel(ERROR) + self.doExtractAndMerge(input, self.m_outputT0, outputFaults0) + self.m_logger.setLevel(INFO) + request.Set(executive.CONTINUE_EXECUTING(), 1) # type: ignore + + if self.m_requestDataStep >= self.m_currentTimeStepIndex: + # displayed time step, no need to go further + request.Remove(executive.CONTINUE_EXECUTING()) # type: ignore + # reinitialize requestDataStep if filter is recalled later + self.m_requestDataStep = -1 + # do extraction and merge + self.doExtractAndMerge(input, outputCells, outputFaults) + # copy attributes from initial time step + for ( + attributeName, + attributeNewName, + ) in getAttributeToTransferFromInitialTime().items(): + copyAttribute( + self.m_outputT0, outputCells, attributeName, attributeNewName + ) + # create elementCenter attribute if needed + cellCenterAttributeName: str = ( + GeosMeshOutputsEnum.ELEMENT_CENTER.attributeName + ) + createCellCenterAttribute(outputCells, cellCenterAttributeName) + + except AssertionError as e: + mess: str = "Block extraction and merge failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Block extraction and merge failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + + return 1 + + def doExtractAndMerge( + self: Self, + input: vtkMultiBlockDataSet, + outputCells: vtkMultiBlockDataSet, + outputFaults: vtkMultiBlockDataSet, + ) -> bool: + """Apply block extraction and merge. + + Args: + input (vtkMultiBlockDataSet): input multi block + outputCells (vtkMultiBlockDataSet): output volume mesh + outputFaults (vtkMultiBlockDataSet): output surface mesh + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + # extract blocks + blockExtractor: GeosBlockExtractor = GeosBlockExtractor() + blockExtractor.SetLogger(self.m_logger) + blockExtractor.SetInputDataObject(input) + blockExtractor.ExtractFaultsOn() + blockExtractor.Update() + + # recover output objects from GeosBlockExtractor filter + volumeBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputVolume() + faultBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputFaults() + + # rename attributes and merge blocks + assert volumeBlockExtracted is not None, "Extracted Volume mesh is null." + outputCells.ShallowCopy(self.mergeBlocksFilter(volumeBlockExtracted, False)) + outputCells.Modified() + + assert faultBlockExtracted is not None, "Extracted Fault mesh is null." + outputFaults.ShallowCopy(self.mergeBlocksFilter(faultBlockExtracted, True)) + outputFaults.Modified() + + self.m_logger.info( + "Volume blocks were successfully splitted from surfaces" + + " and ranks were merged together." + ) + return True + + def mergeBlocksFilter( + self: Self, input: vtkMultiBlockDataSet, convertSurfaces: bool = False + ) -> vtkMultiBlockDataSet: + """Apply vtk merge block filter on input multi block mesh. + + Args: + input (vtkMultiBlockDataSet): multiblock mesh to merge + convertSurfaces (bool, optional): True to convert surface from vtkUnstructuredGrid to + vtkPolyData. Defaults to False. + + Returns: + vtkMultiBlockDataSet: Multiblock mesh composed of internal merged blocks. + """ + mergeBlockFilter = GeosBlockMerge() + mergeBlockFilter.SetLogger(self.m_logger) + mergeBlockFilter.SetInputDataObject(input) + if convertSurfaces: + mergeBlockFilter.ConvertSurfaceMeshOn() + else: + mergeBlockFilter.ConvertSurfaceMeshOff() + mergeBlockFilter.Update() + mergedBlocks: vtkMultiBlockDataSet = mergeBlockFilter.GetOutputDataObject(0) + assert mergedBlocks is not None, "Final merged MultiBlockDataSet is null." + return mergedBlocks diff --git a/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeSurfaceWell.py b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeSurfaceWell.py new file mode 100644 index 00000000..362c921e --- /dev/null +++ b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeSurfaceWell.py @@ -0,0 +1,379 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkMultiBlockDataSet + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.filters.GeosBlockExtractor import GeosBlockExtractor +from geos_posp.filters.GeosBlockMerge import GeosBlockMerge +from geos_posp.processing.vtkUtils import ( + copyAttribute, + createCellCenterAttribute, +) +from geos_posp.utils.GeosOutputsConstants import ( + GeosMeshOutputsEnum, + getAttributeToTransferFromInitialTime, +) +from geos_posp.utils.Logger import ERROR, INFO, Logger, getLogger +from geos_posp.visu.PVUtils.paraviewTreatments import getTimeStepIndex + +__doc__ = """ +PVExtractMergeBlocksVolumeSurfaceWell is a Paraview plugin that allows to merge +ranks of a Geos output objects containing a volumic mesh, surfaces, and wells. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in 3 output pipelines: + +* first pipeline contains the volume mesh. If multiple regions were defined in + the volume mesh, they are preserved as distinct blocks. +* second pipeline contains surfaces. If multiple surfaces were used, they are + preserved as distinct blocks. +* third pipeline contains wells. If multiple wells were used, they are preserved + as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVExtractMergeBlocksVolumeSurfaceWell. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVExtractMergeBlocksVolumeSurfaceWell Filter. + +""" + + +@smproxy.filter( + name="PVExtractMergeBlocksVolumeSurfaceWell", + label="Geos Extract And Merge Blocks - Volume/Surface/Well", +) +@smhint.xml( + """ + + + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVExtractMergeBlocksVolumeSurfaceWell(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to extract and merge ranks from Geos output Mesh. + + To apply in the case of output ".pvd" file contains Volume, Fault and + Well elements. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=3, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: all time steps from input + self.m_timeSteps: npt.NDArray[np.float64] = np.array([]) + #: displayed time step in the IHM + self.m_currentTime: float = 0.0 + #: time step index of displayed time step + self.m_currentTimeStepIndex: int = 0 + #: request data processing step - incremented each time RequestUpdateExtent is called + self.m_requestDataStep: int = -1 + + # saved object at initial time step + self.m_outputT0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + + # set logger + self.m_logger: Logger = getLogger("Extract and merge block Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outDataCells = self.GetOutputData(outInfoVec, 0) + outDataFaults = self.GetOutputData(outInfoVec, 1) + outDataWells = self.GetOutputData(outInfoVec, 2) + assert inData is not None + if outDataCells is None or (not outDataCells.IsA("vtkMultiBlockDataSet")): + outDataCells = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(0).Set( + outDataCells.DATA_OBJECT(), outDataCells # type: ignore + ) + + if outDataFaults is None or (not outDataFaults.IsA("vtkMultiBlockDataSet")): + outDataFaults = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(1).Set( + outDataFaults.DATA_OBJECT(), outDataFaults # type: ignore + ) + + if outDataWells is None or (not outDataWells.IsA("vtkMultiBlockDataSet")): + outDataWells = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(2).Set( + outDataWells.DATA_OBJECT(), outDataWells # type: ignore + ) + + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestUpdateExtent( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestUpdateExtent. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() + inInfo = inInfoVec[0] + # get displayed time step info before updating time + if self.m_requestDataStep == -1: + self.m_logger.info(f"Apply filter {__name__}") + self.m_timeSteps = inInfo.GetInformationObject(0).Get( + executive.TIME_STEPS() # type: ignore + ) + self.m_currentTime = inInfo.GetInformationObject(0).Get( + executive.UPDATE_TIME_STEP() # type: ignore + ) + self.m_currentTimeStepIndex = getTimeStepIndex( + self.m_currentTime, self.m_timeSteps + ) + # update requestDataStep + self.m_requestDataStep += 1 + + # update time according to requestDataStep iterator + inInfo.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), self.m_timeSteps[self.m_requestDataStep] # type: ignore + ) + outInfoVec.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), self.m_timeSteps[self.m_requestDataStep] # type: ignore + ) + + # update all objects according to new time info + self.Modified() + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + outputCells: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 0) + outputFaults: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 1) + outputWells: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 2) + + assert input is not None, "Input MultiBlockDataSet is null." + assert outputCells is not None, "Output volum mesh is null." + assert outputFaults is not None, "Output surface mesh is null." + assert outputWells is not None, "Output well mesh is null." + + # time controller + executive = self.GetExecutive() + if self.m_requestDataStep == 0: + # first time step + # do extraction and merge (do not display phase info) + self.m_logger.setLevel(ERROR) + outputFaults0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + outputWells0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + self.doExtractAndMerge(input, outputCells, outputFaults0, outputWells0) + self.m_logger.setLevel(INFO) + # save input mesh to copy later + self.m_outputT0.ShallowCopy(outputCells) + request.Set(executive.CONTINUE_EXECUTING(), 1) # type: ignore + if self.m_requestDataStep >= self.m_currentTimeStepIndex: + # displayed time step, no need to go further + request.Remove(executive.CONTINUE_EXECUTING()) # type: ignore + # reinitialize requestDataStep if filter is recalled later + self.m_requestDataStep = -1 + # do extraction and merge + self.doExtractAndMerge(input, outputCells, outputFaults, outputWells) + # copy attributes from initial time step + for ( + attributeName, + attributeNewName, + ) in getAttributeToTransferFromInitialTime().items(): + copyAttribute( + self.m_outputT0, outputCells, attributeName, attributeNewName + ) + # create elementCenter attribute in the volume mesh if needed + cellCenterAttributeName: str = ( + GeosMeshOutputsEnum.ELEMENT_CENTER.attributeName + ) + createCellCenterAttribute(outputCells, cellCenterAttributeName) + except AssertionError as e: + mess: str = "Block extraction and merge failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Block extraction and merge failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def doExtractAndMerge( + self: Self, + input: vtkMultiBlockDataSet, + outputCells: vtkMultiBlockDataSet, + outputFaults: vtkMultiBlockDataSet, + outputWells: vtkMultiBlockDataSet, + ) -> bool: + """Apply block extraction and merge. + + Args: + input (vtkMultiBlockDataSet): input multi block + outputCells (vtkMultiBlockDataSet): output volume mesh + outputFaults (vtkMultiBlockDataSet): output surface mesh + outputWells (vtkMultiBlockDataSet): output well mesh + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + # extract blocks + blockExtractor: GeosBlockExtractor = GeosBlockExtractor() + blockExtractor.SetLogger(self.m_logger) + blockExtractor.SetInputDataObject(input) + blockExtractor.ExtractFaultsOn() + blockExtractor.ExtractWellsOn() + blockExtractor.Update() + + # recover output objects from GeosBlockExtractor filter and merge internal blocks + volumeBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputVolume() + assert volumeBlockExtracted is not None, "Extracted Volume mesh is null." + outputCells.ShallowCopy(self.mergeBlocksFilter(volumeBlockExtracted, False)) + + faultBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputFaults() + assert faultBlockExtracted is not None, "Extracted Fault mesh is null." + outputFaults.ShallowCopy(self.mergeBlocksFilter(faultBlockExtracted, True)) + + wellBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputWells() + assert wellBlockExtracted is not None, "Extracted Well mesh is null." + outputWells.ShallowCopy(self.mergeBlocksFilter(wellBlockExtracted, False)) + + outputCells.Modified() + outputFaults.Modified() + outputWells.Modified() + + self.m_logger.info( + "Volume blocks were successfully splitted from surfaces" + + " and wells, and ranks were merged together." + ) + return True + + def mergeBlocksFilter( + self: Self, input: vtkMultiBlockDataSet, convertSurfaces: bool = False + ) -> vtkMultiBlockDataSet: + """Apply vtk merge block filter on input multi block mesh. + + Args: + input (vtkMultiBlockDataSet): multiblock mesh to merge + convertSurfaces (bool, optional): True to convert surface from vtkUnstructuredGrid to + vtkPolyData. Defaults to False. + + Returns: + vtkMultiBlockDataSet: Multiblock mesh composed of internal merged blocks. + """ + mergeBlockFilter = GeosBlockMerge() + mergeBlockFilter.SetLogger(self.m_logger) + mergeBlockFilter.SetInputDataObject(input) + if convertSurfaces: + mergeBlockFilter.ConvertSurfaceMeshOn() + else: + mergeBlockFilter.ConvertSurfaceMeshOff() + mergeBlockFilter.Update() + mergedBlocks: vtkMultiBlockDataSet = mergeBlockFilter.GetOutputDataObject(0) + assert mergedBlocks is not None, "Final merged MultiBlockDataSet is null." + return mergedBlocks diff --git a/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeWell.py b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeWell.py new file mode 100644 index 00000000..28326a21 --- /dev/null +++ b/geos-posp/src/PVplugins/PVExtractMergeBlocksVolumeWell.py @@ -0,0 +1,360 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +import numpy.typing as npt +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkMultiBlockDataSet + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.filters.GeosBlockExtractor import GeosBlockExtractor +from geos_posp.filters.GeosBlockMerge import GeosBlockMerge +from geos_posp.processing.vtkUtils import ( + copyAttribute, + createCellCenterAttribute, +) +from geos_posp.utils.GeosOutputsConstants import ( + GeosMeshOutputsEnum, + getAttributeToTransferFromInitialTime, +) +from geos_posp.utils.Logger import ERROR, INFO, Logger, getLogger +from geos_posp.visu.PVUtils.paraviewTreatments import getTimeStepIndex + +__doc__ = """ +PVExtractMergeBlocksVolumeWell is a Paraview plugin that allows to merge +ranks of a Geos output objects containing a volumic mesh and wells. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in 2 output pipelines: + +* first pipeline contains the volume mesh. If multiple regions were defined in + the volume mesh, they are preserved as distinct blocks. +* second pipeline contains wells. If multiple wells were used, they are preserved + as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVExtractMergeBlocksVolumeWell. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVExtractMergeBlocksVolumeWell Filter. + +""" + + +@smproxy.filter( + name="PVExtractMergeBlocksVolumeWell", + label="Geos Extract And Merge Blocks - Volume/Well", +) +@smhint.xml( + """ + + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVExtractMergeBlocksVolumeWell(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to extract and merge ranks from Geos output Mesh. + + To apply in the case of output ".pvd" file contains Volume and Well + elements. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=2, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: all time steps from input + self.m_timeSteps: npt.NDArray[np.float64] = np.array([]) + #: displayed time step in the IHM + self.m_currentTime: float = 0.0 + #: time step index of displayed time step + self.m_currentTimeStepIndex: int = 0 + #: request data processing step - incremented each time RequestUpdateExtent is called + self.m_requestDataStep: int = -1 + + # saved object at initial time step + self.m_outputT0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + + # set logger + self.m_logger: Logger = getLogger("Extract and merge block Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outDataCells = self.GetOutputData(outInfoVec, 0) + outDataWells = self.GetOutputData(outInfoVec, 1) + assert inData is not None + if outDataCells is None or (not outDataCells.IsA("vtkMultiBlockDataSet")): + outDataCells = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(0).Set( + outDataCells.DATA_OBJECT(), outDataCells # type: ignore + ) + + if outDataWells is None or (not outDataWells.IsA("vtkMultiBlockDataSet")): + outDataWells = vtkMultiBlockDataSet() + outInfoVec.GetInformationObject(1).Set( + outDataWells.DATA_OBJECT(), outDataWells # type: ignore + ) + + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestUpdateExtent( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestUpdateExtent. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() + inInfo = inInfoVec[0] + # get displayed time step info before updating time + if self.m_requestDataStep == -1: + self.m_logger.info(f"Apply filter {__name__}") + self.m_timeSteps = inInfo.GetInformationObject(0).Get( + executive.TIME_STEPS() # type: ignore + ) + self.m_currentTime = inInfo.GetInformationObject(0).Get( + executive.UPDATE_TIME_STEP() # type: ignore + ) + self.m_currentTimeStepIndex = getTimeStepIndex( + self.m_currentTime, self.m_timeSteps + ) + # update requestDataStep + self.m_requestDataStep += 1 + + # update time according to requestDataStep iterator + inInfo.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), self.m_timeSteps[self.m_requestDataStep] # type: ignore + ) + outInfoVec.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), self.m_timeSteps[self.m_requestDataStep] # type: ignore + ) + + # update all objects according to new time info + self.Modified() + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + outputCells: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 0) + outputWells: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 1) + + assert input is not None, "Input MultiBlockDataSet is null." + assert outputCells is not None, "Output volum mesh is null." + assert outputWells is not None, "Output well mesh is null." + + # time controller + executive = self.GetExecutive() + if self.m_requestDataStep == 0: + # first time step + # do extraction and merge (do not display phase info) + self.m_logger.setLevel(ERROR) + outputWells0: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + self.doExtractAndMerge(input, outputCells, outputWells0) + self.m_logger.setLevel(INFO) + # save input mesh to copy later + self.m_outputT0.ShallowCopy(outputCells) + request.Set(executive.CONTINUE_EXECUTING(), 1) # type: ignore + if self.m_requestDataStep >= self.m_currentTimeStepIndex: + # displayed time step, no need to go further + request.Remove(executive.CONTINUE_EXECUTING()) # type: ignore + # reinitialize requestDataStep if filter is recalled later + self.m_requestDataStep = -1 + # do extraction and merge + self.doExtractAndMerge(input, outputCells, outputWells) + # copy attributes from initial time step + for ( + attributeName, + attributeNewName, + ) in getAttributeToTransferFromInitialTime().items(): + copyAttribute( + self.m_outputT0, outputCells, attributeName, attributeNewName + ) + # create elementCenter attribute if needed + cellCenterAttributeName: str = ( + GeosMeshOutputsEnum.ELEMENT_CENTER.attributeName + ) + createCellCenterAttribute(outputCells, cellCenterAttributeName) + + except AssertionError as e: + mess: str = "Block extraction and merge failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Block extraction and merge failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + + return 1 + + def doExtractAndMerge( + self: Self, + input: vtkMultiBlockDataSet, + outputCells: vtkMultiBlockDataSet, + outputWells: vtkMultiBlockDataSet, + ) -> bool: + """Apply block extraction and merge. + + Args: + input (vtkMultiBlockDataSet): input multi block + outputCells (vtkMultiBlockDataSet): output volume mesh + outputWells (vtkMultiBlockDataSet): output well mesh + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + # extract blocks + blockExtractor: GeosBlockExtractor = GeosBlockExtractor() + blockExtractor.SetLogger(self.m_logger) + blockExtractor.SetInputDataObject(input) + blockExtractor.ExtractFaultsOff() + blockExtractor.ExtractWellsOn() + blockExtractor.Update() + + # recover output objects from GeosBlockExtractor filter and merge internal blocks + volumeBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputVolume() + assert volumeBlockExtracted is not None, "Extracted Volume mesh is null." + outputCells.ShallowCopy(self.mergeBlocksFilter(volumeBlockExtracted, False)) + + wellBlockExtracted: vtkMultiBlockDataSet = blockExtractor.getOutputWells() + assert wellBlockExtracted is not None, "Extracted Well mesh is null." + outputWells.ShallowCopy(self.mergeBlocksFilter(wellBlockExtracted, False)) + + outputCells.Modified() + outputWells.Modified() + + self.m_logger.info( + "Volume blocks were successfully splitted from " + + "wells, and ranks were merged together." + ) + return True + + def mergeBlocksFilter( + self: Self, input: vtkMultiBlockDataSet, convertSurfaces: bool = False + ) -> vtkMultiBlockDataSet: + """Apply vtk merge block filter on input multi block mesh. + + Args: + input (vtkMultiBlockDataSet): multiblock mesh to merge + convertSurfaces (bool, optional): True to convert surface from vtkUnstructuredGrid to + vtkPolyData. Defaults to False. + + Returns: + vtkMultiBlockDataSet: Multiblock mesh composed of internal merged blocks. + """ + mergeBlockFilter = GeosBlockMerge() + mergeBlockFilter.SetLogger(self.m_logger) + mergeBlockFilter.SetInputDataObject(input) + if convertSurfaces: + mergeBlockFilter.ConvertSurfaceMeshOn() + else: + mergeBlockFilter.ConvertSurfaceMeshOff() + mergeBlockFilter.Update() + mergedBlocks: vtkMultiBlockDataSet = mergeBlockFilter.GetOutputDataObject(0) + assert mergedBlocks is not None, "Final merged MultiBlockDataSet is null." + return mergedBlocks diff --git a/geos-posp/src/PVplugins/PVGeomechanicsAnalysis.py b/geos-posp/src/PVplugins/PVGeomechanicsAnalysis.py new file mode 100644 index 00000000..7d8662a3 --- /dev/null +++ b/geos-posp/src/PVplugins/PVGeomechanicsAnalysis.py @@ -0,0 +1,386 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +from typing import Union + +import numpy as np +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkPointSet, vtkUnstructuredGrid + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_GRAIN_BULK_MODULUS, + DEFAULT_ROCK_COHESION, + WATER_DENSITY, +) + +__doc__ = """ +PVGeomechanicsAnalysis is a Paraview plugin that allows to compute +additional geomechanical attributes from the input mesh. + +Input and output types are vtkMultiBlockDataSet. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVGeomechanicsAnalysis. +* Select any pipeline child of the first ouput from PVExtractMergeBlocksVolume* filter. +* Search and Apply PVGeomechanicsAnalysis Filter. + +""" + + +@smproxy.filter(name="PVGeomechanicsAnalysis", label="Geos Geomechanics Analysis") +@smhint.xml("""""") +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype( + dataTypes=["vtkUnstructuredGrid", "vtkPointSet"], composite_data_supported=True +) +class PVGeomechanicsAnalysis(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to compute additional geomechanical outputs. + + Input is either a vtkUnstructuredGrid or vtkPointSet with Geos + geomechanical properties. + """ + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkPointSet") + + # outputs and additional parameters + self.m_computeAdvancedOutputs: bool = False + self.m_grainBulkModulus: float = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity: float = WATER_DENSITY + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_DEG + + # set m_logger + self.m_logger: Logger = getLogger("Geomechanics Analysis Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + @smproperty.doublevector( + name="GrainBulkModulus", + label="Grain bulk modulus (Pa)", + default_values=DEFAULT_GRAIN_BULK_MODULUS, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference grain bulk modulus to compute Biot coefficient. + The unit is Pa. Default is Quartz bulk modulus (i.e., 38GPa). + + """ + ) + def b01SetGrainBulkModulus(self: Self, value: float) -> None: + """Set grain bulk modulus. + + Args: + value (float): grain bulk modulus (Pa) + """ + self.m_grainBulkModulus = value + self.Modified() + + def getGrainBulkModulus(self: Self) -> float: + """Access to the grain bulk modulus value. + + Returns: + float: self.m_grainBulkModulus. + """ + return self.m_grainBulkModulus + + @smproperty.doublevector( + name="SpecificDensity", + label="Specific Density (kg/m3)", + default_values=WATER_DENSITY, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference density to compute specific gravity. + The unit is kg/m3. Default is fresh water density (i.e., 1000 kg/m3). + + """ + ) + def b02SetSpecificDensity(self: Self, value: float) -> None: + """Set specific density. + + Args: + value (float): Reference specific density (kg/m3) + """ + self.m_specificDensity = value + self.Modified() + + def getSpecificDensity(self: Self) -> float: + """Access the specific density value. + + Returns: + float: self.m_specificDensity. + """ + return self.m_specificDensity + + @smproperty.xml( + """ + + + + + """ + ) + def b09GroupBasicOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="AdvancedOutputsUse", + label="Compute advanced geomechanical outputs", + default_values=0, + panel_visibility="default", + ) + @smdomain.xml( + """ + + + Check to compute advanced geomechanical outputs including + reservoir stress paths and fracture indexes. + + """ + ) + def c01SetAdvancedOutputs(self: Self, boolean: bool) -> None: + """Set advanced output calculation option. + + Args: + boolean (bool): if True advanced outputs are computed. + """ + self.m_computeAdvancedOutputs = boolean + self.Modified() + + def getComputeAdvancedOutputs(self: Self) -> float: + """Access the advanced outputs option. + + Returns: + float: self.m_computeAdvancedOutputs. + """ + return self.m_computeAdvancedOutputs + + @smproperty.xml( + """ + + panel_visibility="default"> + + """ + ) + def c09GroupAdvancedOutputsUse(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference rock cohesion to compute critical pore pressure. + The unit is Pa.Default is fractured case (i.e., 0. Pa). + + """ + ) + def d01SetRockCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + def getRockCohesion(self: Self) -> float: + """Get rock cohesion. + + Returns: + float: rock cohesion. + """ + return self.m_rockCohesion + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference friction angle to compute critical pore pressure. + The unit is °. Default is no friction case (i.e., 0.°). + + """ + ) + def d02SetFrictionAngle(self: Self, value: float) -> None: + """Set frition angle. + + Args: + value (float): friction angle (°) + """ + self.m_frictionAngle = value + self.Modified() + + def getFrictionAngle(self: Self) -> float: + """Get friction angle in radian. + + Returns: + float: friction angle. + """ + return self.m_frictionAngle * np.pi / 180.0 + + @smproperty.xml( + """ + + + + + + + + """ + ) + def d09GroupAdvancedOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + self.m_logger.info(f"Apply filter {__name__}") + from filters.GeomechanicsCalculator import GeomechanicsCalculator + + inData = self.GetInputData(inInfoVec, 0, 0) + assert inData is not None + + input: Union[vtkPointSet, vtkUnstructuredGrid] + output: Union[vtkPointSet, vtkUnstructuredGrid] + if inData.IsA("vtkUnstructuredGrid"): + input = vtkUnstructuredGrid.GetData(inInfoVec[0]) + output = vtkUnstructuredGrid.GetData(outInfoVec) + elif inData.IsA("vtkPointSet"): + input = vtkPointSet.GetData(inInfoVec[0]) + output = vtkPointSet.GetData(outInfoVec) + else: + raise TypeError("Error type") + + assert input is not None, "Input object is null" + assert output is not None, "Output object is null" + + # create new properties + geomechanicsCalculatorFilter: GeomechanicsCalculator = ( + GeomechanicsCalculator() + ) + geomechanicsCalculatorFilter.SetLogger(self.m_logger) + geomechanicsCalculatorFilter.SetInputDataObject(input) + if self.m_computeAdvancedOutputs: + geomechanicsCalculatorFilter.computeAdvancedOutputsOn() + else: + geomechanicsCalculatorFilter.computeAdvancedOutputsOff() + geomechanicsCalculatorFilter.SetGrainBulkModulus(self.getGrainBulkModulus()) + geomechanicsCalculatorFilter.SetSpecificDensity(self.getSpecificDensity()) + geomechanicsCalculatorFilter.SetRockCohesion(self.getRockCohesion()) + geomechanicsCalculatorFilter.SetFrictionAngle(self.getFrictionAngle()) + geomechanicsCalculatorFilter.Update() + output.ShallowCopy(geomechanicsCalculatorFilter.GetOutputDataObject(0)) + output.Modified() + + except AssertionError as e: + self.m_logger.error(f"{__name__} filter execution failed due to:") + self.m_logger.error(e) + except Exception as e: + self.m_logger.critical(f"{__name__} filter execution failed due to:") + self.m_logger.critical(e, exc_info=True) + return 1 diff --git a/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolume.py b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolume.py new file mode 100644 index 00000000..62545870 --- /dev/null +++ b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolume.py @@ -0,0 +1,403 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import ( + vtkMultiBlockDataSet, +) + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_GRAIN_BULK_MODULUS, + DEFAULT_ROCK_COHESION, + WATER_DENSITY, +) +from PVplugins.PVExtractMergeBlocksVolume import PVExtractMergeBlocksVolume +from PVplugins.PVGeomechanicsAnalysis import PVGeomechanicsAnalysis + +__doc__ = """ +PVGeomechanicsWorkflowVolume is a Paraview plugin that execute multiple filters +to clean GEOS outputs and compute additional geomechanical outputs on volume. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in the volume mesh. If multiple regions were defined in +the volume mesh, they are preserved as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVGeomechanicsWorkflowVolume. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVGeomechanicsWorkflowVolume Filter. + +""" + + +@smproxy.filter( + name="PVGeomechanicsWorkflowVolume", + label="Geos Geomechanics Workflow - Volume only", +) +@smhint.xml( + """ + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVGeomechanicsWorkflowVolume(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to clean and add new outputs Geos output mesh. + + To apply in the case of output ".pvd" file contains only Volume element. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=1, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: ouput volume mesh + self.m_volumeMesh: vtkMultiBlockDataSet + + self.m_computeAdvancedOutputs: bool = False + self.m_grainBulkModulus: float = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity: float = WATER_DENSITY + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + + # set logger + self.m_logger: Logger = getLogger("Geomechanics Workflow Filter") + + @smproperty.doublevector( + name="GrainBulkModulus", + label="Grain bulk modulus (Pa)", + default_values=DEFAULT_GRAIN_BULK_MODULUS, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference grain bulk modulus to compute Biot coefficient. + The unit is Pa. Default is Quartz bulk modulus (i.e., 38GPa). + + """ + ) + def b01SetGrainBulkModulus(self: Self, value: float) -> None: + """Set grain bulk modulus. + + Args: + value (float): grain bulk modulus (Pa) + """ + self.m_grainBulkModulus = value + self.Modified() + + def getGrainBulkModulus(self: Self) -> float: + """Access to the grain bulk modulus value. + + Returns: + float: self.m_grainBulkModulus. + """ + return self.m_grainBulkModulus + + @smproperty.doublevector( + name="SpecificDensity", + label="Specific Density (kg/m3)", + default_values=WATER_DENSITY, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference density to compute specific gravity. + The unit is kg/m3. Default is fresh water density (i.e., 1000 kg/m3). + + """ + ) + def b02SetSpecificDensity(self: Self, value: float) -> None: + """Set specific density. + + Args: + value (float): Reference specific density (kg/m3) + """ + self.m_specificDensity = value + self.Modified() + + def getSpecificDensity(self: Self) -> float: + """Access the specific density value. + + Returns: + float: self.m_specificDensity. + """ + return self.m_specificDensity + + @smproperty.xml( + """ + + + + + """ + ) + def b09GroupBasicOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="AdvancedOutputsUse", + label="Compute advanced geomechanical outputs", + default_values=0, + panel_visibility="default", + ) + @smdomain.xml( + """ + + + Check to compute advanced geomechanical outputs including + reservoir stress paths and fracture indexes. + + """ + ) + def c01SetAdvancedOutputs(self: Self, boolean: bool) -> None: + """Set advanced output calculation option. + + Args: + boolean (bool): if True advanced outputs are computed. + """ + self.m_computeAdvancedOutputs = boolean + self.Modified() + + def getComputeAdvancedOutputs(self: Self) -> float: + """Access the advanced outputs option. + + Returns: + float: self.m_computeAdvancedOutputs. + """ + return self.m_computeAdvancedOutputs + + @smproperty.xml( + """ + + panel_visibility="default"> + + """ + ) + def c09GroupAdvancedOutputsUse(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference rock cohesion to compute critical pore pressure. + The unit is Pa.Default is fractured case (i.e., 0. Pa). + + """ + ) + def d01SetRockCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + def getRockCohesion(self: Self) -> float: + """Get rock cohesion. + + Returns: + float: rock cohesion. + """ + return self.m_rockCohesion + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference friction angle to compute critical pore pressure. + The unit is °. Default is 10°. + + """ + ) + def d02SetFrictionAngle(self: Self, value: float) -> None: + """Set frition angle. + + Args: + value (float): friction angle (°) + """ + self.m_frictionAngle = value * np.pi / 180.0 + self.Modified() + + def getFrictionAngle(self: Self) -> float: + """Get friction angle in radian. + + Returns: + float: friction angle. + """ + return self.m_frictionAngle + + @smproperty.xml( + """ + + + + + + + + """ + ) + def d09GroupAdvancedOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo: vtkInformation = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + self.m_volumeMesh = self.GetOutputData(outInfoVec, 0) + + assert input is not None, "Input MultiBlockDataSet is null." + assert self.m_volumeMesh is not None, "Output volume mesh is null." + + # 1. extract volume + self.doExtractAndMerge() + # 2. compute Geomechanical outputs in volume mesh + self.computeAdditionalOutputsVolume() + + except AssertionError as e: + mess: str = "Geomechanics workflow failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Geomechanics workflow failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def doExtractAndMerge(self: Self) -> bool: + """Apply block extraction and merge filter. + + Args: + input (vtkMultiBlockDataSet): input multi block + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + filter: PVExtractMergeBlocksVolume = PVExtractMergeBlocksVolume() + filter.SetInputConnection(self.GetInputConnection(0, 0)) + filter.SetLogger(self.m_logger) + filter.Update() + + # recover output objects from PVExtractMergeBlocksVolume + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_volumeMesh.Modified() + return True + + def computeAdditionalOutputsVolume(self: Self) -> bool: + """Compute geomechanical outputs on the volume mesh. + + Returns: + bool: True if calculation successfully eneded, False otherwise. + """ + filter = PVGeomechanicsAnalysis() + filter.SetInputDataObject(self.m_volumeMesh) + filter.b01SetGrainBulkModulus(self.getGrainBulkModulus()) + filter.b02SetSpecificDensity(self.getSpecificDensity()) + filter.d01SetRockCohesion(self.getRockCohesion()) + filter.d02SetFrictionAngle(self.getFrictionAngle()) + filter.c01SetAdvancedOutputs(self.m_computeAdvancedOutputs) + filter.SetLogger(self.m_logger) + filter.Update() + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_volumeMesh.Modified() + return True diff --git a/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeSurface.py b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeSurface.py new file mode 100644 index 00000000..e835b1fd --- /dev/null +++ b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeSurface.py @@ -0,0 +1,420 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import ( + vtkMultiBlockDataSet, +) + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_GRAIN_BULK_MODULUS, + DEFAULT_ROCK_COHESION, + WATER_DENSITY, +) +from PVplugins.PVExtractMergeBlocksVolumeSurface import ( + PVExtractMergeBlocksVolumeSurface, +) +from PVplugins.PVGeomechanicsAnalysis import PVGeomechanicsAnalysis +from PVplugins.PVSurfaceGeomechanics import PVSurfaceGeomechanics + +__doc__ = """ +PVGeomechanicsWorkflowVolumeSurface is a Paraview plugin that execute +multiple filters to clean GEOS outputs and compute additional geomechanical +outputs on volume and surface. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in 2 output pipelines: + +* first pipeline contains the volume mesh. If multiple regions were defined in + the volume mesh, they are preserved as distinct blocks. +* second pipeline contains surfaces. If multiple surfaces were used, they are + preserved as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVGeomechanicsWorkflowVolumeSurface. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVGeomechanicsWorkflowVolumeSurface Filter. + +""" + + +@smproxy.filter( + name="PVGeomechanicsWorkflowVolumeSurface", + label="Geos Geomechanics Workflow - Volume/Surface", +) +@smhint.xml( + """ + + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVGeomechanicsWorkflowVolumeSurface(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to clean and add new outputs Geos output mesh. + + To apply in the case of output ".pvd" file contains Volume and Fault + elements. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=2, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: ouput volume mesh + self.m_volumeMesh: vtkMultiBlockDataSet + #: output surface mesh + self.m_surfaceMesh: vtkMultiBlockDataSet + + self.m_computeAdvancedOutputs: bool = False + self.m_grainBulkModulus: float = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity: float = WATER_DENSITY + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + + # set logger + self.m_logger: Logger = getLogger("Geomechanics Workflow Filter") + + @smproperty.doublevector( + name="GrainBulkModulus", + label="Grain bulk modulus (Pa)", + default_values=DEFAULT_GRAIN_BULK_MODULUS, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference grain bulk modulus to compute Biot coefficient. + The unit is Pa. Default is Quartz bulk modulus (i.e., 38GPa). + + """ + ) + def b01SetGrainBulkModulus(self: Self, value: float) -> None: + """Set grain bulk modulus. + + Args: + value (float): grain bulk modulus (Pa) + """ + self.m_grainBulkModulus = value + self.Modified() + + def getGrainBulkModulus(self: Self) -> float: + """Access to the grain bulk modulus value. + + Returns: + float: self.m_grainBulkModulus. + """ + return self.m_grainBulkModulus + + @smproperty.doublevector( + name="SpecificDensity", + label="Specific Density (kg/m3)", + default_values=WATER_DENSITY, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference density to compute specific gravity. + The unit is kg/m3. Default is fresh water density (i.e., 1000 kg/m3). + + """ + ) + def b02SetSpecificDensity(self: Self, value: float) -> None: + """Set specific density. + + Args: + value (float): Reference specific density (kg/m3) + """ + self.m_specificDensity = value + self.Modified() + + def getSpecificDensity(self: Self) -> float: + """Access the specific density value. + + Returns: + float: self.m_specificDensity. + """ + return self.m_specificDensity + + @smproperty.xml( + """ + + + + + """ + ) + def b09GroupBasicOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference rock cohesion to compute critical pore pressure. + The unit is Pa.Default is fractured case (i.e., 0. Pa). + + """ + ) + def d01SetRockCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + def getRockCohesion(self: Self) -> float: + """Get rock cohesion. + + Returns: + float: rock cohesion. + """ + return self.m_rockCohesion + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference friction angle to compute critical pore pressure. + The unit is °. Default is 10°. + + """ + ) + def d02SetFrictionAngle(self: Self, value: float) -> None: + """Set frition angle. + + Args: + value (float): friction angle (°) + """ + self.m_frictionAngle = value * np.pi / 180.0 + self.Modified() + + def getFrictionAngle(self: Self) -> float: + """Get friction angle in radian. + + Returns: + float: friction angle. + """ + return self.m_frictionAngle + + @smproperty.xml( + """ + + + + + """ + ) + def d09GroupAdvancedOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="AdvancedOutputsUse", + label="Compute advanced geomechanical volume outputs", + default_values=0, + panel_visibility="default", + ) + @smdomain.xml( + """ + + + Check to compute advanced geomechanical outputs including + reservoir stress paths and fracture indexes. + + """ + ) + def e01SetAdvancedOutputs(self: Self, boolean: bool) -> None: + """Set advanced output calculation option. + + Args: + boolean (bool): if True advanced outputs are computed. + """ + self.m_computeAdvancedOutputs = boolean + self.Modified() + + def getComputeAdvancedOutputs(self: Self) -> float: + """Access the advanced outputs option. + + Returns: + float: self.m_computeAdvancedOutputs. + """ + return self.m_computeAdvancedOutputs + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo: vtkInformation = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + self.m_volumeMesh = self.GetOutputData(outInfoVec, 0) + self.m_surfaceMesh = self.GetOutputData(outInfoVec, 1) + + assert input is not None, "Input MultiBlockDataSet is null." + assert self.m_volumeMesh is not None, "Output volume mesh is null." + assert self.m_surfaceMesh is not None, "Output surface mesh is null." + + # 1. extract volume/surface + self.doExtractAndMerge() + # 2. compute Geomechanical outputs in volume mesh + self.computeAdditionalOutputsVolume() + # 3. compute geomechanical outputs on surface mesh + self.computeSurfaceGeomecanics() + + except AssertionError as e: + mess: str = "Geomechanics workflow failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Geomechanics workflow failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def doExtractAndMerge(self: Self) -> bool: + """Apply block extraction and merge filter. + + Args: + input (vtkMultiBlockDataSet): input multi block + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + filter: PVExtractMergeBlocksVolumeSurface = PVExtractMergeBlocksVolumeSurface() + filter.SetInputConnection(self.GetInputConnection(0, 0)) + filter.SetLogger(self.m_logger) + filter.Update() + + # recover output objects from PVExtractMergeBlocksVolumeSurface + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_surfaceMesh.ShallowCopy(filter.GetOutputDataObject(1)) + self.m_volumeMesh.Modified() + self.m_surfaceMesh.Modified() + return True + + def computeAdditionalOutputsVolume(self: Self) -> bool: + """Compute geomechanical outputs on the volume mesh. + + Returns: + bool: True if calculation successfully eneded, False otherwise. + """ + filter = PVGeomechanicsAnalysis() + filter.SetInputDataObject(self.m_volumeMesh) + filter.b01SetGrainBulkModulus(self.getGrainBulkModulus()) + filter.b02SetSpecificDensity(self.getSpecificDensity()) + filter.d01SetRockCohesion(self.getRockCohesion()) + filter.d02SetFrictionAngle(self.getFrictionAngle()) + filter.c01SetAdvancedOutputs(self.m_computeAdvancedOutputs) + filter.SetLogger(self.m_logger) + filter.Update() + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_volumeMesh.Modified() + return True + + def computeSurfaceGeomecanics(self: Self) -> bool: + """Compute surface geomechanics new attributes. + + Returns: + bool: True if calculation successfully eneded, False otherwise. + """ + filter = PVSurfaceGeomechanics() + filter.SetInputDataObject(self.m_surfaceMesh) + filter.a01SetRockCohesion(self.getRockCohesion()) + filter.a02SetFrictionAngle(self.getFrictionAngle()) + filter.SetLogger(self.m_logger) + filter.Update() + self.m_surfaceMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_surfaceMesh.Modified() + return True diff --git a/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeSurfaceWell.py b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeSurfaceWell.py new file mode 100644 index 00000000..45334d1d --- /dev/null +++ b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeSurfaceWell.py @@ -0,0 +1,431 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import ( + vtkMultiBlockDataSet, +) + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_GRAIN_BULK_MODULUS, + DEFAULT_ROCK_COHESION, + WATER_DENSITY, +) +from PVplugins.PVExtractMergeBlocksVolumeSurfaceWell import ( + PVExtractMergeBlocksVolumeSurfaceWell, +) +from PVplugins.PVGeomechanicsAnalysis import PVGeomechanicsAnalysis +from PVplugins.PVSurfaceGeomechanics import PVSurfaceGeomechanics + +__doc__ = """ +PVGeomechanicsWorkflowVolumeSurfaceWell is a Paraview plugin that execute +multiple filters to clean GEOS outputs and compute additional geomechanical +outputs on volume, surface and wells. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in 3 output pipelines: + +* first pipeline contains the volume mesh. If multiple regions were defined in + the volume mesh, they are preserved as distinct blocks. +* second pipeline contains surfaces. If multiple surfaces were used, they are + preserved as distinct blocks. +* third pipeline contains wells. If multiple wells were used, they are preserved + as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVGeomechanicsWorkflowVolumeSurfaceWell. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVGeomechanicsWorkflowVolumeSurfaceWell Filter. + +""" + + +@smproxy.filter( + name="PVGeomechanicsWorkflowVolumeSurfaceWell", + label="Geos Geomechanics Workflow - Volume/Surface/Well", +) +@smhint.xml( + """ + + + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVGeomechanicsWorkflowVolumeSurfaceWell(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to clean and add new outputs Geos output mesh. + + To apply in the case of output ".pvd" file contains Volume, Fault and + Well elements. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=3, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: ouput volume mesh + self.m_volumeMesh: vtkMultiBlockDataSet + #: output surface mesh + self.m_surfaceMesh: vtkMultiBlockDataSet + #: output wells + self.m_wells: vtkMultiBlockDataSet + + self.m_computeAdvancedOutputs: bool = False + self.m_grainBulkModulus: float = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity: float = WATER_DENSITY + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + + # set logger + self.m_logger: Logger = getLogger("Geomechanics Workflow Filter") + + @smproperty.doublevector( + name="GrainBulkModulus", + label="Grain bulk modulus (Pa)", + default_values=DEFAULT_GRAIN_BULK_MODULUS, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference grain bulk modulus to compute Biot coefficient. + The unit is Pa. Default is Quartz bulk modulus (i.e., 38GPa). + + """ + ) + def b01SetGrainBulkModulus(self: Self, value: float) -> None: + """Set grain bulk modulus. + + Args: + value (float): grain bulk modulus (Pa) + """ + self.m_grainBulkModulus = value + self.Modified() + + def getGrainBulkModulus(self: Self) -> float: + """Access to the grain bulk modulus value. + + Returns: + float: self.m_grainBulkModulus. + """ + return self.m_grainBulkModulus + + @smproperty.doublevector( + name="SpecificDensity", + label="Specific Density (kg/m3)", + default_values=WATER_DENSITY, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference density to compute specific gravity. + The unit is kg/m3. Default is fresh water density (i.e., 1000 kg/m3). + + """ + ) + def b02SetSpecificDensity(self: Self, value: float) -> None: + """Set specific density. + + Args: + value (float): Reference specific density (kg/m3) + """ + self.m_specificDensity = value + self.Modified() + + def getSpecificDensity(self: Self) -> float: + """Access the specific density value. + + Returns: + float: self.m_specificDensity. + """ + return self.m_specificDensity + + @smproperty.xml( + """ + + + + + """ + ) + def b09GroupBasicOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference rock cohesion to compute critical pore pressure. + The unit is Pa.Default is fractured case (i.e., 0. Pa). + + """ + ) + def d01SetRockCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + def getRockCohesion(self: Self) -> float: + """Get rock cohesion. + + Returns: + float: rock cohesion. + """ + return self.m_rockCohesion + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference friction angle to compute critical pore pressure. + The unit is °. Default is 10°. + + """ + ) + def d02SetFrictionAngle(self: Self, value: float) -> None: + """Set frition angle. + + Args: + value (float): friction angle (°) + """ + self.m_frictionAngle = value * np.pi / 180.0 + self.Modified() + + def getFrictionAngle(self: Self) -> float: + """Get friction angle in radian. + + Returns: + float: friction angle. + """ + return self.m_frictionAngle + + @smproperty.xml( + """ + + + + + """ + ) + def d09GroupAdvancedOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="AdvancedOutputsUse", + label="Compute advanced geomechanical volume outputs", + default_values=0, + panel_visibility="default", + ) + @smdomain.xml( + """ + + + Check to compute advanced geomechanical outputs including + reservoir stress paths and fracture indexes. + + """ + ) + def e01SetAdvancedOutputs(self: Self, boolean: bool) -> None: + """Set advanced output calculation option. + + Args: + boolean (bool): if True advanced outputs are computed. + """ + self.m_computeAdvancedOutputs = boolean + self.Modified() + + def getComputeAdvancedOutputs(self: Self) -> float: + """Access the advanced outputs option. + + Returns: + float: self.m_computeAdvancedOutputs. + """ + return self.m_computeAdvancedOutputs + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo: vtkInformation = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + self.m_volumeMesh = self.GetOutputData(outInfoVec, 0) + self.m_surfaceMesh = self.GetOutputData(outInfoVec, 1) + self.m_wells = self.GetOutputData(outInfoVec, 2) + + assert input is not None, "Input MultiBlockDataSet is null." + assert self.m_volumeMesh is not None, "Output volume mesh is null." + assert self.m_surfaceMesh is not None, "Output surface mesh is null." + assert self.m_wells is not None, "Output well mesh is null." + + # 1. extract volume/surface/wells + self.doExtractAndMerge() + # 2. compute Geomechanical outputs in volume mesh + self.computeAdditionalOutputsVolume() + # 3. compute geomechanical outputs on surface mesh + self.computeSurfaceGeomecanics() + + except AssertionError as e: + mess: str = "Geomechanics workflow failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Geomechanics workflow failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def doExtractAndMerge(self: Self) -> bool: + """Apply block extraction and merge filter. + + Args: + input (vtkMultiBlockDataSet): input multi block + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + filter: PVExtractMergeBlocksVolumeSurfaceWell = ( + PVExtractMergeBlocksVolumeSurfaceWell() + ) + filter.SetInputConnection(self.GetInputConnection(0, 0)) + filter.SetLogger(self.m_logger) + filter.Update() + + # recover output objects from PVExtractMergeBlocksVolumeSurfaceWell + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_surfaceMesh.ShallowCopy(filter.GetOutputDataObject(1)) + self.m_wells.ShallowCopy(filter.GetOutputDataObject(2)) + self.m_volumeMesh.Modified() + self.m_surfaceMesh.Modified() + self.m_wells.Modified() + return True + + def computeAdditionalOutputsVolume(self: Self) -> bool: + """Compute geomechanical outputs on the volume mesh. + + Returns: + bool: True if calculation successfully eneded, False otherwise. + """ + filter = PVGeomechanicsAnalysis() + filter.SetInputDataObject(self.m_volumeMesh) + filter.b01SetGrainBulkModulus(self.getGrainBulkModulus()) + filter.b02SetSpecificDensity(self.getSpecificDensity()) + filter.d01SetRockCohesion(self.getRockCohesion()) + filter.d02SetFrictionAngle(self.getFrictionAngle()) + filter.c01SetAdvancedOutputs(self.m_computeAdvancedOutputs) + filter.SetLogger(self.m_logger) + filter.Update() + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_volumeMesh.Modified() + return True + + def computeSurfaceGeomecanics(self: Self) -> bool: + """Compute surface geomechanics new attributes. + + Returns: + bool: True if calculation successfully eneded, False otherwise. + """ + filter = PVSurfaceGeomechanics() + filter.SetInputDataObject(self.m_surfaceMesh) + filter.a01SetRockCohesion(self.getRockCohesion()) + filter.a02SetFrictionAngle(self.getFrictionAngle()) + filter.SetLogger(self.m_logger) + filter.Update() + self.m_surfaceMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_surfaceMesh.Modified() + return True diff --git a/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeWell.py b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeWell.py new file mode 100644 index 00000000..74e722d7 --- /dev/null +++ b/geos-posp/src/PVplugins/PVGeomechanicsWorkflowVolumeWell.py @@ -0,0 +1,418 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import ( + vtkMultiBlockDataSet, +) + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) + +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_GRAIN_BULK_MODULUS, + DEFAULT_ROCK_COHESION, + WATER_DENSITY, +) +from PVplugins.PVExtractMergeBlocksVolumeWell import ( + PVExtractMergeBlocksVolumeWell, +) +from PVplugins.PVGeomechanicsAnalysis import PVGeomechanicsAnalysis + +__doc__ = """ +PVGeomechanicsWorkflowVolumeWell is a Paraview plugin that execute +multiple filters to clean GEOS outputs and compute additional geomechanical +outputs on volume and wells. + +Input and output types are vtkMultiBlockDataSet. + +This filter results in 2 output pipelines: + +* first pipeline contains the volume mesh. If multiple regions were defined in + the volume mesh, they are preserved as distinct blocks. +* second pipeline contains wells. If multiple wells were used, they are preserved + as distinct blocks. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVGeomechanicsWorkflowVolumeWell. +* Select the Geos output .pvd file loaded in Paraview. +* Search and Apply PVGeomechanicsWorkflowVolumeWell Filter. + +""" + + +@smproxy.filter( + name="PVGeomechanicsWorkflowVolumeWell", + label="Geos Geomechanics Workflow - Volume/Well", +) +@smhint.xml( + """ + + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVGeomechanicsWorkflowVolumeWell(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to clean and add new outputs Geos output mesh. + + To apply in the case of output ".pvd" file contains Volume and + Well elements. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=2, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + #: ouput volume mesh + self.m_volumeMesh: vtkMultiBlockDataSet + #: output wells + self.m_wells: vtkMultiBlockDataSet + + self.m_computeAdvancedOutputs: bool = False + self.m_grainBulkModulus: float = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity: float = WATER_DENSITY + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + + # set logger + self.m_logger: Logger = getLogger("Geomechanics Workflow Filter") + + @smproperty.doublevector( + name="GrainBulkModulus", + label="Grain bulk modulus (Pa)", + default_values=DEFAULT_GRAIN_BULK_MODULUS, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference grain bulk modulus to compute Biot coefficient. + The unit is Pa. Default is Quartz bulk modulus (i.e., 38GPa). + + """ + ) + def b01SetGrainBulkModulus(self: Self, value: float) -> None: + """Set grain bulk modulus. + + Args: + value (float): grain bulk modulus (Pa) + """ + self.m_grainBulkModulus = value + self.Modified() + + def getGrainBulkModulus(self: Self) -> float: + """Access to the grain bulk modulus value. + + Returns: + float: self.m_grainBulkModulus. + """ + return self.m_grainBulkModulus + + @smproperty.doublevector( + name="SpecificDensity", + label="Specific Density (kg/m3)", + default_values=WATER_DENSITY, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference density to compute specific gravity. + The unit is kg/m3. Default is fresh water density (i.e., 1000 kg/m3). + + """ + ) + def b02SetSpecificDensity(self: Self, value: float) -> None: + """Set specific density. + + Args: + value (float): Reference specific density (kg/m3) + """ + self.m_specificDensity = value + self.Modified() + + def getSpecificDensity(self: Self) -> float: + """Access the specific density value. + + Returns: + float: self.m_specificDensity. + """ + return self.m_specificDensity + + @smproperty.xml( + """ + + + + + """ + ) + def b09GroupBasicOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="AdvancedOutputsUse", + label="Compute advanced geomechanical outputs", + default_values=0, + panel_visibility="default", + ) + @smdomain.xml( + """ + + + Check to compute advanced geomechanical outputs including + reservoir stress paths and fracture indexes. + + """ + ) + def c01SetAdvancedOutputs(self: Self, boolean: bool) -> None: + """Set advanced output calculation option. + + Args: + boolean (bool): if True advanced outputs are computed. + """ + self.m_computeAdvancedOutputs = boolean + self.Modified() + + def getComputeAdvancedOutputs(self: Self) -> float: + """Access the advanced outputs option. + + Returns: + float: self.m_computeAdvancedOutputs. + """ + return self.m_computeAdvancedOutputs + + @smproperty.xml( + """ + + panel_visibility="default"> + + """ + ) + def c09GroupAdvancedOutputsUse(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference rock cohesion to compute critical pore pressure. + The unit is Pa.Default is fractured case (i.e., 0. Pa). + + """ + ) + def d01SetRockCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + def getRockCohesion(self: Self) -> float: + """Get rock cohesion. + + Returns: + float: rock cohesion. + """ + return self.m_rockCohesion + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference friction angle to compute critical pore pressure. + The unit is °. Default is 10°. + + """ + ) + def d02SetFrictionAngle(self: Self, value: float) -> None: + """Set frition angle. + + Args: + value (float): friction angle (°) + """ + self.m_frictionAngle = value * np.pi / 180.0 + self.Modified() + + def getFrictionAngle(self: Self) -> float: + """Get friction angle in radian. + + Returns: + float: friction angle. + """ + return self.m_frictionAngle + + @smproperty.xml( + """ + + + + + + + + """ + ) + def d09GroupAdvancedOutputParameters(self: Self) -> None: + """Organize groups.""" + self.Modified() + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo: vtkInformation = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + self.m_volumeMesh = self.GetOutputData(outInfoVec, 0) + self.m_wells = self.GetOutputData(outInfoVec, 1) + + assert input is not None, "Input MultiBlockDataSet is null." + assert self.m_volumeMesh is not None, "Output volume mesh is null." + assert self.m_wells is not None, "Output well mesh is null." + + # 1. extract volume/wells + self.doExtractAndMerge() + # 2. compute Geomechanical outputs in volume mesh + self.computeAdditionalOutputsVolume() + + except AssertionError as e: + mess: str = "Geomechanics workflow failed due to:" + self.m_logger.error(mess) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess1: str = "Geomechanics workflow failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def doExtractAndMerge(self: Self) -> bool: + """Apply block extraction and merge filter. + + Args: + input (vtkMultiBlockDataSet): input multi block + + Returns: + bool: True if extraction and merge successfully eneded, False otherwise + """ + filter: PVExtractMergeBlocksVolumeWell = PVExtractMergeBlocksVolumeWell() + filter.SetInputConnection(self.GetInputConnection(0, 0)) + filter.SetLogger(self.m_logger) + filter.Update() + + # recover output objects from PVExtractMergeBlocksVolumeWell + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_wells.ShallowCopy(filter.GetOutputDataObject(1)) + self.m_volumeMesh.Modified() + self.m_wells.Modified() + return True + + def computeAdditionalOutputsVolume(self: Self) -> bool: + """Compute geomechanical outputs on the volume mesh. + + Returns: + bool: True if calculation successfully eneded, False otherwise. + """ + filter = PVGeomechanicsAnalysis() + filter.SetInputDataObject(self.m_volumeMesh) + filter.b01SetGrainBulkModulus(self.getGrainBulkModulus()) + filter.b02SetSpecificDensity(self.getSpecificDensity()) + filter.d01SetRockCohesion(self.getRockCohesion()) + filter.d02SetFrictionAngle(self.getFrictionAngle()) + filter.c01SetAdvancedOutputs(self.m_computeAdvancedOutputs) + filter.SetLogger(self.m_logger) + filter.Update() + self.m_volumeMesh.ShallowCopy(filter.GetOutputDataObject(0)) + self.m_volumeMesh.Modified() + return True diff --git a/geos-posp/src/PVplugins/PVGeosLogReader.py b/geos-posp/src/PVplugins/PVGeosLogReader.py new file mode 100644 index 00000000..b35cb1c6 --- /dev/null +++ b/geos-posp/src/PVplugins/PVGeosLogReader.py @@ -0,0 +1,624 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +from enum import Enum +from typing import Union, cast + +import numpy as np +import numpy.typing as npt +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import vtkmodules.util.numpy_support as vnp +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtk import VTK_DOUBLE # type: ignore[import-untyped] +from vtkmodules.vtkCommonCore import vtkDataArraySelection as vtkDAS +from vtkmodules.vtkCommonCore import ( + vtkDoubleArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import vtkTable + +from geos_posp.processing.geosLogReaderFunctions import ( + identifyProperties, + transformUserChoiceToListPhases, +) +from geos_posp.readers.GeosLogReaderAquifers import GeosLogReaderAquifers +from geos_posp.readers.GeosLogReaderConvergence import GeosLogReaderConvergence +from geos_posp.readers.GeosLogReaderFlow import GeosLogReaderFlow +from geos_posp.readers.GeosLogReaderWells import GeosLogReaderWells +from geos_posp.utils.enumUnits import ( + Mass, + MassRate, + Pressure, + Time, + Unit, + Volume, + VolumetricRate, + enumerationDomainUnit, +) +from geos_posp.utils.UnitRepository import UnitRepository +from geos_posp.visu.PVUtils.checkboxFunction import ( # type: ignore[attr-defined] + createModifiedCallback, +) +from geos_posp.visu.PVUtils.paraviewTreatments import ( + strListToEnumerationDomainXml, +) + +__doc__ = """ +GeosLogRePVGeosLogReaderader is a Paraview plugin that allows to read Geos output log. + +Input is a file and output is a vtkTable containing log information. + +..WARNING:: + + The reader is compliant with GEOS log before commit version #9365098. + For more recent version, use the csv or hdf5 export options from GEOS. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVGeosLogReader. +* Open (File>Open...) and Select Geos output log .out/.txt file. +* In the "Open data with..." window, Select PVGeosLogReader reader. + +""" + + +@smproxy.reader( + name="PVGeosLogReader", + label="Geos Log Reader", + extensions=["txt", "out"], + file_description="txt and out files of GEOS log files", +) +class PVGeosLogReader(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview reader for Geos log files ."txt" or ".out". + + Output is a vtkTable with data extracted from the log. + """ + super().__init__(nInputPorts=0, nOutputPorts=1, outputType="vtkTable") + self.m_filepath: str = "" + self.m_phasesUserChoice: list[str] = [] + self.m_dataframeChoice: int = 0 + self.m_dataframe: pd.DataFrame + self.m_numberWellsMean: int = 1 + + # checkboxes values + self.m_useSIUnits: int = 0 + self.m_pressureUnit: int = 0 + self.m_bhpUnit: int = 0 + self.m_stressUnit: int = 0 + self.m_timeUnit: int = 0 + self.m_massUnit: int = 0 + self.m_volumeUnit: int = 0 + self.m_volumetricRateUnit: int = 0 + self.m_massRateUnit: int = 0 + self.m_densityUnit: int = 0 + + # for selection of properties + self.m_propertiesFlow: vtkDAS = vtkDAS() + self.m_propertiesFlow.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + propsFlow: list[str] = [ + "DeltaPressure", + "Pressure", + "Temperature", + "TotalDynamicPoreVolume", + "DynamicPoreVolumes", + "NonTrapped", + "Trapped", + "Immobile", + "Mobile", + "Dissolved", + "TotalFluidMass", + "CellFluidMass", + ] + for prop in propsFlow: + self.m_propertiesFlow.AddArray(prop) + + self.m_propertiesWells: vtkDAS = vtkDAS() + self.m_propertiesWells.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + propsWells: list[str] = [ + "MeanBHP", + "MeanTotalMassRate", + "MeanTotalVolumetricRate", + "MeanSurfaceVolumetricRate", + "TotalMassRate", + "TotalVolumetricRate", + "SurfaceVolumetricRate", + "Mass", + "BHP", + ] + for prop in propsWells: + self.m_propertiesWells.AddArray(prop) + + self.m_propertiesAquifers: vtkDAS = vtkDAS() + self.m_propertiesAquifers.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + propsAquifers: list[str] = [ + "Volume", + "VolumetricRate", + "CumulatedVolume", + "CumulatedVolumetricRate", + ] + for prop in propsAquifers: + self.m_propertiesAquifers.AddArray(prop) + + self.m_convergence: vtkDAS = vtkDAS() + self.m_convergence.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + propsSolvers: list[str] = ["NewtonIter", "LinearIter"] + for prop in propsSolvers: + self.m_convergence.AddArray(prop) + + @smproperty.stringvector( + name="DataFilepath", default_values="Enter a filepath to your data" + ) + @smdomain.filelist() + @smhint.filechooser(extensions=["txt", "out"], file_description="Data files") + def a01SetFilepath(self: Self, filepath: str) -> None: + """Set Geos log file path. + + Args: + filepath (str): path to the file. + + Raises: + FileNotFoundError: file not found. + """ + if filepath != "Enter a filepath to your data": + if not os.path.exists(filepath): + raise FileNotFoundError(f"Invalid filepath {filepath}") + else: + self.m_filepath = filepath + self.Modified() + + def getFilepath(self: Self) -> str: + """Get Geos log file path. + + Returns: + str: filepath. + """ + return self.m_filepath + + @smproperty.stringvector( + name="EnterPhaseNames", label="Enter Phase Names", default_values="" + ) + @smdomain.xml( + """ + Please enter your phase names as phase0, phase1, phase2. + """ + ) + def a02SetPhaseNames(self: Self, value: str) -> None: + """Set phase names. + + Args: + value (str): list of phase names seprated by space. + """ + self.m_phasesUserChoice = transformUserChoiceToListPhases(value) + self.Modified() + + def getPhasesUserChoice(self: Self) -> list[str]: + """Access the phases from the user input. + + Returns: + list[str]: phase names. + """ + return self.m_phasesUserChoice + + @smproperty.intvector( + name="DataframeChoice", + number_of_elements=1, + label="DataframeChoice", + default_values=0, + ) + @smdomain.xml( + strListToEnumerationDomainXml(["Flow", "Wells", "Aquifers", "Convergence"]) + ) + def a03SetDataFrameChoice(self: Self, value: int) -> None: + """Set reader choice: 0:Flow, 1:Wells, 2:Aquifers, 3:Convergence. + + Args: + value (int): user choice. + """ + self.m_dataframeChoice = value + self.Modified() + + def getDataframeChoice(self: Self) -> int: + """Accesses the choice of dataframe from the user. + + Returns: + int: The value corresponding to a certain dataframe. + "Flow" has value "0", "Wells" has value "1", + "Aquifers" has value "2", "Convergence" has + value "3". + """ + return self.m_dataframeChoice + + @smproperty.xml( + """ + + + + """ + ) + def a04PropertyGroup(self: Self) -> None: + """Organized group.""" + self.Modified() + + @smproperty.dataarrayselection(name="FlowProperties") + def a05SetPropertiesFlow(self: Self) -> vtkDAS: + """Use Flow.""" + return self.m_propertiesFlow + + @smproperty.xml( + """ + + + """ + ) + def a06GroupFlow(self: Self) -> None: + """Organized group.""" + self.Modified() + + @smproperty.dataarrayselection(name="WellsProperties") + def a07SetPropertiesWells(self: Self) -> vtkDAS: + """Use wells.""" + return self.m_propertiesWells + + @smproperty.intvector(name="NumberOfWellsForMeanCalculation", default_values=1) + def a08SetTheNumberOfWellsMean(self: Self, number: int) -> None: + """Set number of wells. + + Args: + number (int): number of wells. + """ + self.m_numberWellsMean = number + self.Modified() + + def getNumberOfWellsMean(self: Self) -> int: + """Get the number of wells. + + Returns: + int: The number of wells to consider. + """ + return self.m_numberWellsMean + + @smproperty.xml( + """ + + + + """ + ) + def a09GroupWells(self: Self) -> None: + """Organized group.""" + self.Modified() + + @smproperty.dataarrayselection(name="AquifersProperties") + def a10SetPropertiesAquifers(self: Self) -> vtkDAS: + """Use aquifers.""" + return self.m_propertiesAquifers + + @smproperty.xml( + """ + + + """ + ) + def a11GroupAquifers(self: Self) -> None: + """Organized group.""" + self.Modified() + + @smproperty.dataarrayselection(name="Convergence") + def a12SetConvergence(self: Self) -> vtkDAS: + """Use convergence.""" + return self.m_convergence + + @smproperty.xml( + """ + + + """ + ) + def a13GroupSolvers(self: Self) -> None: + """Organized group.""" + self.Modified() + + def getIdsToUse(self: Self) -> list[str]: + """Get property ids. + + Using the checkbox choices of the user for metaproperties, + we get the list of ids to map the dataframe properties with the + properties. + + Returns: + list(str): Ids of the metaproperties. + """ + dataArrays: dict[int, vtkDAS] = { + 0: self.m_propertiesFlow, + 1: self.m_propertiesWells, + 2: self.m_propertiesAquifers, + 3: self.m_convergence, + } + dataArrayToUse = dataArrays[self.getDataframeChoice()] + propertyNames: list[str] = [] + for i in range(dataArrayToUse.GetNumberOfArrays()): + propName: str = dataArrayToUse.GetArrayName(i) + if dataArrayToUse.ArrayIsEnabled(propName) == 1: + propertyNames.append(propName) + propertiesWithId: list[str] = identifyProperties(propertyNames) + onlyIds: list[str] = [] + for propId in propertiesWithId: + idFound: str = propId.split(":")[0] + onlyIds.append(idFound) + return onlyIds + + @smproperty.intvector(name="UseSIUnits", label="UseSIUnits", default_values=1) + @smdomain.xml("""""") + def b01SetUseSIUnits(self: Self, value: int) -> None: + """Set Use SI Units. + + Args: + value (int): user choice. + """ + self.m_useSIUnits = value + self.Modified() + + @smproperty.intvector( + name="Pressure", label="Pressure", default_values=0, panel_visibility="default" + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, Pressure))) + def b02SetPressureUnit(self: Self, value: int) -> None: + """Set pressure unit. + + Args: + value (int): user choice. + """ + self.m_pressureUnit = value + self.Modified() + + @smproperty.intvector( + name="BHP", label="BHP", default_values=0, panel_visibility="default" + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, Pressure))) + def b03SetBHPUnit(self: Self, value: int) -> None: + """Set BHP unit. + + Args: + value (int): user choice. + """ + self.m_bhpUnit = value + self.Modified() + + @smproperty.intvector( + name="Time", label="Time", default_values=0, panel_visibility="default" + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, Time))) + def b04SetTimeUnit(self: Self, value: int) -> None: + """Set time unit. + + Args: + value (int): user choice. + """ + self.m_timeUnit = value + self.Modified() + + @smproperty.intvector( + name="Mass", label="Mass", default_values=0, panel_visibility="default" + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, Mass))) + def b05SetMassUnit(self: Self, value: int) -> None: + """Set mass unit. + + Args: + value (int): user choice. + """ + self.m_massUnit = value + self.Modified() + + @smproperty.intvector( + name="Volume", label="Volume", default_values=0, panel_visibility="default" + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, Volume))) + def b06SetVolumeUnit(self: Self, value: int) -> None: + """Set volume unit. + + Args: + value (int): user choice. + """ + self.m_volumeUnit = value + self.Modified() + + @smproperty.intvector( + name="VolumetricRate", + label="VolumetricRate", + default_values=0, + panel_visibility="default", + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, VolumetricRate))) + def b07SetVolumetricRateUnit(self: Self, value: int) -> None: + """Set volumetric rate unit. + + Args: + value (int): user choice. + """ + self.m_volumetricRateUnit = value + self.Modified() + + @smproperty.intvector( + name="MassRate", label="MassRate", default_values=0, panel_visibility="default" + ) + @smdomain.xml(enumerationDomainUnit(cast(Enum, MassRate))) + def b08SetMassRateUnit(self: Self, value: int) -> None: + """Set Mass rate unit. + + Args: + value (int): user choice. + """ + """""" + self.m_massRateUnit = value + self.Modified() + + @smproperty.xml( + """ + + + + + + + + + """ + ) + def b09GroupUnitsToUse(self: Self) -> None: + """Organize group.""" + self.Modified() + + def getUseSIUnits(self: Self) -> int: + """Acess the choice to use SI units or not. + + Returns: + int: 0 to not use SI units or 1 to use SI units. + """ + return self.m_useSIUnits + + def getUnitChoices(self: Self) -> dict[str, int]: + """Get the units choosen by the user. + + Based on the choice of using SI units or not, and if + not with the units chosen by the user, returns a dict + with metaproperties such as pressure, volume etc ... + with the unit associated. + + Returns: + dict[str, int]: empty dictionary if use SI unit, or + property name as keys and unit choice as values. + """ + unitChoices: dict[str, int] = {} + if not self.getUseSIUnits(): + unitChoices = { + "pressure": self.m_pressureUnit, + "stress": self.m_stressUnit, + "bhp": self.m_bhpUnit, + "mass": self.m_massUnit, + "massRate": self.m_massRateUnit, + "time": self.m_timeUnit, + "volume": self.m_volumeUnit, + "volumetricRate": self.m_volumetricRateUnit, + "density": self.m_densityUnit, + } + return unitChoices + + def createDataframe(self: Self) -> pd.DataFrame: + """Create dataframe with values from Geos log based on user choices. + + Returns: + pd.DataFrame: Dataframe with log values according to user choice. + """ + filepath: str = self.getFilepath() + phaseNames: list[str] = self.getPhasesUserChoice() + choice: int = self.getDataframeChoice() + userPropertiesUnits: dict[str, int] = self.getUnitChoices() + unitObj: UnitRepository = UnitRepository(userPropertiesUnits) + propertiesUnit: dict[str, Unit] = unitObj.getPropertiesUnit() + reader: Union[ + GeosLogReaderFlow, + GeosLogReaderWells, + GeosLogReaderAquifers, + GeosLogReaderConvergence, + ] + if choice == 0: + reader = GeosLogReaderFlow(filepath, propertiesUnit, phaseNames) + elif choice == 1: + nbrWells: int = self.getNumberOfWellsMean() + reader = GeosLogReaderWells(filepath, propertiesUnit, phaseNames, nbrWells) + elif choice == 2: + reader = GeosLogReaderAquifers(filepath, propertiesUnit) + elif choice == 3: + reader = GeosLogReaderConvergence(filepath, propertiesUnit) + return reader.createDataframe() + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() + outInfo = outInfoVec.GetInformationObject(0) + outInfo.Remove(executive.TIME_STEPS()) + outInfo.Remove(executive.TIME_RANGE()) + return 1 + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + # we choose which dataframe to build and get it + idsToUse = self.getIdsToUse() + dataframe = self.createDataframe() + usefulColumns = [] + for column_name in list(dataframe.columns): + if ":" not in column_name: + usefulColumns.append(column_name) + else: + idFound = column_name.split(":")[0] + if idFound in idsToUse: + usefulColumns.append(column_name) + # we build the output vtkTable + output: vtkTable = vtkTable.GetData(outInfoVec, 0) + for column in usefulColumns: + pandas_series: pd.Series = dataframe[column] + array: npt.NDArray[np.float64] = pandas_series.values + if ":" in column: + column = column.split(":")[1] + + newAttr: vtkDoubleArray = vnp.numpy_to_vtk(array, deep=True, array_type=VTK_DOUBLE) # type: ignore[no-untyped-call] + newAttr.SetName(column) + output.AddColumn(newAttr) + except Exception as e: + print("Error while reading Geos log file:") + print(str(e)) + return 0 + return 1 diff --git a/geos-posp/src/PVplugins/PVMergeBlocksEnhanced.py b/geos-posp/src/PVplugins/PVMergeBlocksEnhanced.py new file mode 100644 index 00000000..034bc7dd --- /dev/null +++ b/geos-posp/src/PVplugins/PVMergeBlocksEnhanced.py @@ -0,0 +1,121 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +from typing_extensions import Self, Union + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtkmodules.vtkCommonCore import ( + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCompositeDataSet, + vtkMultiBlockDataSet, + vtkUnstructuredGrid, +) + +from geos_posp.processing.vtkUtils import mergeBlocks +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +Merge filter that keep partial attributes using nan values. + +Input is a vtkMultiBlockDataSet and output is a vtkUnstructuredGrid. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVMergeBlocksEnhanced. +* Select the mesh you want to create the attributes and containing a region attribute. +* Search and Apply Merge Blocks Keeping Partial Attributes Filter. + +""" + + +@smproxy.filter( + name="PVMergeBlocksEnhanced", label="Merge Blocks Keeping Partial Attributes" +) +@smhint.xml('') +@smproperty.input(name="Input", port_index=0, label="Input") +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVMergeBlocksEnhanced(VTKPythonAlgorithmBase): + + def __init__(self: Self) -> None: + """Merge filter that keep partial attributes using nan values.""" + super().__init__( + nInputPorts=1, + nOutputPorts=1, + inputType="vtkMultiBlockDataSet", + outputType="vtkUnstructuredGrid", + ) + + # logger + self.m_logger: Logger = getLogger("Merge Filter Enhanced") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + self.Modified() + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + + self.m_logger.info(f"Apply filter {__name__}") + try: + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet] = self.GetInputData( + inInfoVec, 0, 0 + ) + output: vtkUnstructuredGrid = vtkUnstructuredGrid.GetData(outInfoVec) + + assert input is not None, "Input mesh is null." + assert output is not None, "Output pipeline is null." + + output0 = mergeBlocks(input, True) + output.ShallowCopy(output0) + output.Modified() + + mess: str = f"Blocks were successfully merged together." + self.m_logger.info(mess) + except AssertionError as e: + mess1: str = "Block merge failed due to:" + self.m_logger.error(mess1) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Block merge failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 diff --git a/geos-posp/src/PVplugins/PVMohrCirclePlot.py b/geos-posp/src/PVplugins/PVMohrCirclePlot.py new file mode 100644 index 00000000..ca5a438f --- /dev/null +++ b/geos-posp/src/PVplugins/PVMohrCirclePlot.py @@ -0,0 +1,879 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +from enum import Enum +from typing import Any, Union, cast + +import numpy as np +import numpy.typing as npt +from paraview.simple import ( # type: ignore[import-not-found] + Render, +) +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from typing_extensions import Self +from vtkmodules.vtkCommonCore import vtkDataArraySelection as vtkDAS +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import ( + vtkMultiBlockDataSet, + vtkUnstructuredGrid, +) + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import geos_posp.visu.mohrCircles.functionsMohrCircle as mcf +import geos_posp.visu.PVUtils.paraviewTreatments as pvt +from geos_posp.processing.MohrCircle import MohrCircle +from geos_posp.processing.vtkUtils import getArrayInObject, mergeBlocks +from geos_posp.utils.enumUnits import Pressure, enumerationDomainUnit +from geos_posp.utils.GeosOutputsConstants import ( + FAILURE_ENVELOPE, + GeosMeshOutputsEnum, +) +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_ROCK_COHESION, +) +from geos_posp.visu.PVUtils.checkboxFunction import ( # type: ignore[attr-defined] + createModifiedCallback, +) +from geos_posp.visu.PVUtils.DisplayOrganizationParaview import ( + buildNewLayoutWithPythonView, +) +from geos_posp.visu.PVUtils.matplotlibOptions import ( + FontStyleEnum, + FontWeightEnum, + LegendLocationEnum, + LineStyleEnum, + MarkerStyleEnum, + OptionSelectionEnum, + optionEnumToXml, +) + +__doc__ = """ +PVMohrCirclePlot is a Paraview plugin that allows to compute and plot +Mohr's circles of selected cells and times from effective stress attribute. + +Input is a vtkMultiBlockDataSet or vtkUnstructuredGrid. + +This filter results in opening a new Python View window and displaying +Mohr's circle plot. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVMohrCirclePlot. +* Select the mesh containing the cells you want to plot Mohr's circles. +* Search and Apply Mohr's Circle Plot Filter. + +.. WARNING:: + Input vtk must contains a limited number of cells, Paraview may crash + otherwise. In addition, input pipeline should consist of the minimum number + of filters since this filter repeats the operations at every time steps. + +""" + + +@smproxy.filter(name="PVMohrCirclePlot", label="Plot Mohr's Circles") +@smhint.xml( + """ + + + """ +) +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype( + dataTypes=["vtkUnstructuredGrid", "vtkMultiBlockDataSet"], + composite_data_supported=False, +) +class PVMohrCirclePlot(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to plot Mohr's Circles of selected cells and times. + + Mohr's circles are plotted using a Python View. + """ + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkDataObject") + + # create a new PythonView + self.m_pythonView: Any = buildNewLayoutWithPythonView() + + #: list of all cell ids + self.m_cellIds: list[str] = [] + + #: cell selection object + self.m_cellIdsDAS: vtkDAS = vtkDAS() + self.m_cellIdsDAS.AddObserver(0, createModifiedCallback(self)) + + #: list of all time steps + self.m_timeSteps: npt.NDArray[np.float64] = np.array([]) + + #: time steps selection object + self.m_timeStepsDAS: vtkDAS = vtkDAS() + self.m_timeStepsDAS.AddObserver( + 0, createModifiedCallback(self) + ) # type: ignore[arg-type] + + #: list of all mohr circles + self.m_mohrCircles: list[MohrCircle] = [] + + #: failure envelop parameters + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + + #: stress convention (False for GEOS convention) + self.m_stressConvention: bool = False + + #: curve aspect options - the same variables are set for each selected curve + self.m_circleIdUsed: str = "" + self.m_color: tuple[float, float, float] = (0.0, 0.0, 0.0) + self.m_lineStyle: str = LineStyleEnum.SOLID.optionValue + self.m_lineWidth: float = 1.0 + self.m_markerStyle: str = MarkerStyleEnum.NONE.optionValue + self.m_markerSize: float = 1.0 + + #: figure user choices + self.m_userChoices: dict[str, Any] = { + "xAxis": "Normal stress", + "yAxis": "Shear stress", + "stressUnit": 0, + "annotateCircles": 1, + "displayTitle": True, + "title": "Mohr's circles", + "titleStyle": FontStyleEnum.NORMAL.optionValue, + "titleWeight": FontWeightEnum.BOLD.optionValue, + "titleSize": 12, + "displayLegend": True, + "legendPosition": LegendLocationEnum.BEST.optionValue, + "legendSize": 10, + "minorticks": False, + "curvesAspect": {}, + "customAxisLim": False, + "limMinX": None, + "limMaxX": None, + "limMinY": None, + "limMaxY": None, + } + + #: request data processing step - incremented each time RequestUpdateExtent is called + self.m_requestDataStep: int = -1 + + #: logger + self.m_logger: Logger = getLogger("Mohr's Circle Analysis Filter") + + def getUserChoices(self: Self) -> dict[str, Any]: + """Access the m_userChoices attribute. + + Returns: + dict[str] : the user choices for the figure. + """ + return self.m_userChoices + + def getCircleIds(self: Self) -> list[str]: + """Get circle ids to plot. + + Returns: + list[str]: list of circle ids to plot. + """ + cellIds: list[str] = pvt.getArrayChoices(self.a01GetCellIdsDAS()) + timeSteps: list[str] = pvt.getArrayChoices(self.a02GetTimestepsToPlot()) + return [ + mcf.getMohrCircleId(cellId, timeStep) + for timeStep in timeSteps + for cellId in cellIds + ] + + def defineCurvesAspect(self: Self) -> None: + """Add curve aspect parameters according to user choices.""" + self.m_userChoices["curvesAspect"][self.m_circleIdUsed] = { + "color": self.m_color, + "linestyle": self.m_lineStyle, + "linewidth": self.m_lineWidth, + "marker": self.m_markerStyle, + "markersize": self.m_markerSize, + } + + @smproperty.xml( + """ + + + Recompute all the Mohr's circles at all time steps and display + selected ones. + + """ + ) + def a00RefreshData(self: Self) -> None: + """Reset self.m_requestDataStep to reload data from all time steps.""" + self.m_requestDataStep = -1 + self.Modified() + + @smproperty.dataarrayselection(name="CellIdToPlot") + def a01GetCellIdsDAS(self: Self) -> vtkDAS: + """Get selected cell ids to plot. + + Returns: + vtkDataArraySelection: selected cell ids. + """ + return self.m_cellIdsDAS + + @smproperty.dataarrayselection(name="TimeStepsToPlot") + def a02GetTimestepsToPlot(self: Self) -> vtkDAS: + """Get selected time steps to plot. + + Returns: + vtkDataArraySelection: selected time steps. + """ + return self.m_timeStepsDAS + + @smproperty.xml( + """ + + + """ + ) + def a03GroupTimesteps(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + ) + def b01SetCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + ) + def b02SetFrictionAngle(self: Self, value: float) -> None: + """Set friction angle. + + Args: + value (float): friction angle (°). + """ + self.m_frictionAngle = value * np.pi / 180.0 + self.Modified() + + @smproperty.xml( + """ + + + """ + ) + def b03GroupUnit(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector(name="StressUnit", label="Stress Unit", default_values=0) + @smdomain.xml(enumerationDomainUnit(cast(Enum, Pressure))) + def b04SetStressUnit(self: Self, choice: int) -> None: + """Set stress unit. + + Args: + choice (int): stress unit index in Pressure enum. + """ + self.m_userChoices["stressUnit"] = choice + self.Modified() + + @smproperty.intvector( + name="StressConventionForCompression", + label="Change stress Convention", + default_values=0, + ) + @smdomain.xml("""""") + def b05SetStressCompressionConvention(self: Self, boolean: bool) -> None: + """Set stress compression convention in plots. + + Args: + boolean (bool): False is same as Geos convention, True is usual + geomechanical convention. + """ + # need to convert Geos results if use the usual convention + self.m_stressConvention = boolean + self.Modified() + + @smproperty.intvector( + name="AnnotateCircles", label="Annotate Circles", default_values=1 + ) + @smdomain.xml("""""") + def b06SetAnnotateCircles(self: Self, boolean: bool) -> None: + """Set option to add annotatations to circles. + + Args: + boolean (bool): user choce. + """ + self.m_userChoices["annotateCircles"] = boolean + self.Modified() + + @smproperty.intvector(name="Minorticks", label="Minorticks", default_values=0) + @smdomain.xml("""""") + def b07SetMinorticks(self: Self, boolean: bool) -> None: + """Set option to display minor ticks. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["minorticks"] = boolean + self.Modified() + + @smproperty.xml( + """ + + + + + """ + ) + def b08GroupUnit(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="ModifyTitleAndLegend", label="Modify Title And Legend", default_values=0 + ) + @smdomain.xml("""""") + def c00SetModifyTitleAndLegend(self: Self, boolean: bool) -> None: + """Set option to modify legend and title. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["displayTitle"] = boolean + self.m_modifyTitleAndLegend = boolean + + @smproperty.stringvector(name="Title", default_values="Mohr's circle") + def c01SetTitlePlot(self: Self, title: str) -> None: + """Set title. + + Args: + title (str): title. + """ + self.m_userChoices["title"] = title + self.Modified() + + @smproperty.intvector(name="Title Style", label="Title Style", default_values=0) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, FontStyleEnum))) + def c02SetTitleStyle(self: Self, value: int) -> None: + """Set title font style. + + Args: + value (int): title font style index in FontStyleEnum. + """ + choice = list(FontStyleEnum)[value] + self.m_userChoices["titleStyle"] = choice.optionValue + self.Modified() + + @smproperty.intvector(name="Title Weight", label="Title Weight", default_values=1) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, FontWeightEnum))) + def c03SetTitleWeight(self: Self, value: int) -> None: + """Set title font weight. + + Args: + value (int): title font weight index in FontWeightEnum. + """ + choice = list(FontWeightEnum)[value] + self.m_userChoices["titleWeight"] = choice.optionValue + self.Modified() + + @smproperty.intvector(name="Title Size", label="Title Size", default_values=12) + @smdomain.xml("""""") + def c04SetTitleSize(self: Self, size: float) -> None: + """Set title font size. + + Args: + size (float): title font size between 1 and 50. + """ + self.m_userChoices["titleSize"] = size + self.Modified() + + @smproperty.xml( + """ + + + + + + """ + ) + def c06PropertyGroup(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="LegendPosition", label="Legend Position", default_values=0 + ) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, LegendLocationEnum))) + def d01SetLegendPosition(self: Self, value: int) -> None: + """Set legend position. + + Args: + value (int): legend position index in LegendLocationEnum. + """ + choice = list(LegendLocationEnum)[value] + self.m_userChoices["legendPosition"] = choice.optionValue + self.Modified() + + @smproperty.intvector(name="LegendSize", label="Legend Size", default_values=10) + @smdomain.xml("""""") + def d02SetLegendSize(self: Self, size: float) -> None: + """Set legend font size. + + Args: + size (float): legend font size between 1 and 50. + """ + self.m_userChoices["legendSize"] = size + self.Modified() + + @smproperty.xml( + """ + + + + """ + ) + def d03PropertyGroup(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.intvector( + name="CustomAxisLim", label="Modify Axis Limits", default_values=0 + ) + @smdomain.xml("""""") + def e01SetCustomAxisLim(self: Self, boolean: bool) -> None: + """Set option to define axis limits. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["customAxisLim"] = boolean + self.Modified() + + @smproperty.doublevector(name="LimMinX", label="X min", default_values=-1e36) + def e02LimMinX(self: Self, value: float) -> None: + """Set X axis min. + + Args: + value (float): X axis min. + """ + value2: Union[float, None] = value + if value2 == -1e36: + value2 = None + self.m_userChoices["limMinX"] = value2 + self.Modified() + + @smproperty.doublevector(name="LimMaxX", label="X max", default_values=1e36) + def e03LimMaxX(self: Self, value: float) -> None: + """Set X axis max. + + Args: + value (float): X axis max. + """ + value2: Union[float, None] = value + if value2 == 1e36: + value2 = None + self.m_userChoices["limMaxX"] = value2 + self.Modified() + + @smproperty.doublevector(name="LimMinY", label="Y min", default_values=-1e36) + def e04LimMinY(self: Self, value: float) -> None: + """Set Y axis min. + + Args: + value (float): Y axis min. + """ + value2: Union[float, None] = value + if value2 == -1e36: + value2 = None + self.m_userChoices["limMinY"] = value2 + self.Modified() + + @smproperty.doublevector(name="LimMaxY", label="Y max", default_values=1e36) + def e05LimMaxY(self: Self, value: float) -> None: + """Set Y axis max. + + Args: + value (float): Y axis max. + """ + value2: Union[float, None] = value + if value2 == 1e36: + value2 = None + self.m_userChoices["limMaxY"] = value2 + self.Modified() + + @smproperty.xml( + """ + + + + + + """ + ) + def e06GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector( + name="ModifyCurvesAspect", label="Modify Curves Aspect", default_values=0 + ) + @smdomain.xml("""""") + def f01SetModifyCurvesAspect(self: Self, boolean: bool) -> None: + """Set option to modify curve aspect. + + Args: + boolean (bool): user choice. + """ + self.m_modifyCurvesAspect = boolean + + @smproperty.stringvector(name="CurvesInfo", information_only="1") + def f02GetCurveNames(self: Self) -> list[str]: + """Get curves to modify. + + Returns: + list[str]: curves to modify + """ + circleIds: list[str] = self.getCircleIds() + return [FAILURE_ENVELOPE] + circleIds + + @smproperty.stringvector( + name="CurveToModify", label="Curve name", number_of_elements="1" + ) + @smdomain.xml( + """ + + + """ + ) + def f03SetCellID(self: Self, value: str) -> None: + """Set circle ids to use. + + Args: + value (str): circle ids. + """ + self.m_circleIdUsed = value + self.Modified() + + @smproperty.intvector(name="LineStyle", label="Line Style", default_values=1) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, LineStyleEnum))) + def f04SetLineStyle(self: Self, value: int) -> None: + """Set line style. + + Args: + value (int): line style index in LineStyleEnum + """ + choice = list(LineStyleEnum)[value] + self.m_lineStyle = choice.optionValue + self.Modified() + + @smproperty.doublevector(name="LineWidth", default_values=1.0) + @smdomain.xml("""""") + def f05SetLineWidth(self: Self, value: float) -> None: + """Set line width. + + Args: + value (float): line width between 1 and 10. + """ + self.m_lineWidth = value + self.Modified() + + @smproperty.intvector(name="MarkerStyle", label="Marker Style", default_values=0) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, MarkerStyleEnum))) + def f06SetMarkerStyle(self: Self, value: int) -> None: + """Set marker style. + + Args: + value (int): Marker style index in MarkerStyleEnum + """ + choice = list(MarkerStyleEnum)[value] + self.m_markerStyle = choice.optionValue + self.Modified() + + @smproperty.doublevector(name="MarkerSize", default_values=1.0) + @smdomain.xml("""""") + def f07SetMarkerSize(self: Self, value: float) -> None: + """Set marker size. + + Args: + value (float): size of markers between 1 and 30. + """ + self.m_markerSize = value + self.Modified() + + @smproperty.xml( + """ + + + + + + + + """ + ) + def f08PropertyGroup(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.doublevector( + name="ColorEnvelop", default_values=[0, 0, 0], number_of_elements=3 + ) + @smdomain.xml("""""") + def f09SetColor(self: Self, value0: float, value1: float, value2: float) -> None: + """Set envelope color. + + Args: + value0 (float): Red color between 0 and 1. + value1 (float): Green color between 0 and 1. + value2 (float): Blue color between 0 and 1. + """ + self.m_color = (value0, value1, value2) + self.Modified() + + @smproperty.xml( + """ + + + """ + ) + def f10PropertyGroup(self: Self) -> None: + """Organize groups.""" + self.Modified() + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + inInfo = inInfoVec[0] + # only at initialization step, no change later + if self.m_requestDataStep < 0: + # get cell ids + inData = self.GetInputData(inInfoVec, 0, 0) + self.m_cellIds = pvt.getVtkOriginalCellIds(inData) + + # update vtkDAS + for circleId in self.m_cellIds: + if not self.m_cellIdsDAS.ArrayExists(circleId): + self.m_cellIdsDAS.AddArray(circleId) + + self.m_timeSteps = inInfo.GetInformationObject(0).Get(executive.TIME_STEPS()) # type: ignore + for timestep in self.m_timeSteps: + if not self.m_timeStepsDAS.ArrayExists(str(timestep)): + self.m_timeStepsDAS.AddArray(str(timestep)) + return 1 + + def RequestUpdateExtent( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestUpdateExtent. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + self.m_logger.info(f"Apply filter {__name__}") + executive = self.GetExecutive() + inInfo = inInfoVec[0] + + if self.m_requestDataStep < 0: + self.m_mohrCircles.clear() + + # update requestDataStep + self.m_requestDataStep += 1 + + # update time according to requestDataStep iterator + if self.m_requestDataStep < len(self.m_timeSteps): + inInfo.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), # type: ignore[no-any-return] + self.m_timeSteps[self.m_requestDataStep], + ) + outInfoVec.GetInformationObject(0).Set( + executive.UPDATE_TIME_STEP(), # type: ignore[no-any-return] + self.m_timeSteps[self.m_requestDataStep], + ) + + # update all objects according to new time info + self.Modified() + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if (outData is None) or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, # noqa: F841 + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: Union[vtkUnstructuredGrid, vtkMultiBlockDataSet] = self.GetInputData( + inInfoVec, 0, 0 + ) + assert input is not None, "Input data is undefined" + + executive = self.GetExecutive() + # get mohr circles from all time steps + if self.m_requestDataStep < len(self.m_timeSteps): + request.Set(executive.CONTINUE_EXECUTING(), 1) # type: ignore[no-any-return] + currentTimeStep: float = ( + inInfoVec[0] + .GetInformationObject(0) + .Get(executive.UPDATE_TIME_STEP()) # type: ignore[no-any-return] + ) + self.m_mohrCircles.extend( + self.createMohrCirclesAtTimeStep(input, currentTimeStep) + ) + + # plot mohr circles + else: + # displayed time step, no need to go further + request.Remove(executive.CONTINUE_EXECUTING()) # type: ignore[no-any-return] + + assert self.m_pythonView is not None, "No Python View was found." + self.defineCurvesAspect() + mohrCircles: list[MohrCircle] = self.filterMohrCircles() + self.m_pythonView.Script = mcf.buildPythonViewScript( + parent_dir_path, + mohrCircles, + self.m_rockCohesion, + self.m_frictionAngle, + self.getUserChoices(), + ) + Render() + + except Exception as e: + self.m_logger.error("Mohr circles cannot be plotted due to:") + self.m_logger.error(str(e)) + return 0 + return 1 + + def createMohrCirclesAtTimeStep( + self: Self, + mesh: Union[vtkUnstructuredGrid, vtkMultiBlockDataSet], + currentTimeStep: float, + ) -> list[MohrCircle]: + """Create mohr circles of all cells at the current time step. + + Args: + mesh (Union[vtkUnstructuredGrid, vtkMultiBlockDataSet]): input mesh. + currentTimeStep (float): current time step + + Returns: + list[MohrCircle]: list of MohrCircles for the current time step. + """ + # get mesh and merge if needed + meshMerged: vtkUnstructuredGrid + if isinstance(mesh, vtkMultiBlockDataSet): + meshMerged = mergeBlocks(mesh) + else: + meshMerged = mesh + + assert meshMerged is not None, "Input data is undefined" + + stressArray: npt.NDArray[np.float64] = getArrayInObject( + meshMerged, GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName, False + ) + return mcf.createMohrCircleAtTimeStep( + stressArray, self.m_cellIds, str(currentTimeStep), self.m_stressConvention + ) + + def filterMohrCircles(self: Self) -> list[MohrCircle]: + """Filter the list of all MohrCircle to get those to plot. + + Returns: + list[MohrCircle]: list of MohrCircle to plot. + """ + # circle ids to plot + circleIds: list[str] = self.getCircleIds() + return [ + mohrCircle + for mohrCircle in self.m_mohrCircles + if mohrCircle.getCircleId() in circleIds + ] diff --git a/geos-posp/src/PVplugins/PVPythonViewConfigurator.py b/geos-posp/src/PVplugins/PVPythonViewConfigurator.py new file mode 100644 index 00000000..9d63e707 --- /dev/null +++ b/geos-posp/src/PVplugins/PVPythonViewConfigurator.py @@ -0,0 +1,929 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +from typing import Any, Union, cast + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.simple import ( # type: ignore[import-not-found] + GetActiveSource, + GetActiveView, + Render, + Show, + servermanager, +) +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtkmodules.vtkCommonCore import ( + vtkDataArraySelection, + vtkInformation, + vtkInformationVector, +) + +import geos_posp.visu.PVUtils.paraviewTreatments as pvt +from geos_posp.visu.PVUtils.checkboxFunction import ( # type: ignore[attr-defined] + createModifiedCallback, +) +from geos_posp.visu.PVUtils.DisplayOrganizationParaview import ( + DisplayOrganizationParaview, +) +from geos_posp.visu.PVUtils.matplotlibOptions import ( + FontStyleEnum, + FontWeightEnum, + LegendLocationEnum, + LineStyleEnum, + MarkerStyleEnum, + OptionSelectionEnum, + optionEnumToXml, +) + +__doc__ = """ +PVPythonViewConfigurator is a Paraview plugin that allows to create cross-plots +from input data using the PythonView. + +Input type is vtkDataObject. + +This filter results in opening a new Python View window and displaying cross-plot. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVPythonViewConfigurator. +* Select the vtkDataObject containing the data to plot. +* Search and Apply PVPythonViewConfigurator Filter. + +""" + + +@smproxy.filter(name="PVPythonViewConfigurator", label="Python View Configurator") +@smhint.xml('') +@smproperty.input(name="Input") +@smdomain.datatype(dataTypes=["vtkDataObject"], composite_data_supported=True) +class PVPythonViewConfigurator(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to create cross-plots in a Python View. + + Input is a vtkDataObject. + """ + super().__init__(nInputPorts=1, nOutputPorts=1) + # python view layout and object + self.m_layoutName: str = "" + self.m_pythonView: Any + self.m_organizationDisplay = DisplayOrganizationParaview() + self.buildNewLayoutWithPythonView() + + # input source and curve names + inputSource = GetActiveSource() + dataset = servermanager.Fetch(inputSource) + dataframe: pd.DataFrame = pvt.vtkToDataframe(dataset) + self.m_pathPythonViewScript: str = os.path.join( + parent_dir_path, "visu/pythonViewUtils/mainPythonView.py" + ) + + # checkboxes + self.m_modifyInputs: int = 1 + self.m_modifyCurves: int = 1 + self.m_multiplyCurves: int = 0 + + # checkboxes curves available from the data of pipeline + self.m_validSources = vtkDataArraySelection() + self.m_curvesToPlot = vtkDataArraySelection() + self.m_curvesMinus1 = vtkDataArraySelection() + self.m_validSources.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + self.m_curvesToPlot.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + self.m_curvesMinus1.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + validSourceNames: set[str] = pvt.getPossibleSourceNames() + for sourceName in validSourceNames: + self.m_validSources.AddArray(sourceName) + validColumnsDataframe: list[str] = list(dataframe.columns) + for name in list(dataframe.columns): + for axis in ["X", "Y", "Z"]: + if "Points" + axis in name and "Points" + axis + "__" in name: + positionDoublon: int = validColumnsDataframe.index("Points" + axis) + validColumnsDataframe.pop(positionDoublon) + break + self.m_validColumnsDataframe: list[str] = sorted( + validColumnsDataframe, key=lambda x: x.lower() + ) + for curveName in validColumnsDataframe: + self.m_curvesToPlot.AddArray(curveName) + self.m_curvesMinus1.AddArray(curveName) + self.m_validSources.DisableAllArrays() + self.m_curvesToPlot.DisableAllArrays() + self.m_curvesMinus1.DisableAllArrays() + self.m_curveToUse: str = "" + # to change the aspects of curves + self.m_curvesToModify: set[str] = pvt.integrateSourceNames( + validSourceNames, set(validColumnsDataframe) + ) + self.m_color: tuple[float, float, float] = (0.0, 0.0, 0.0) + self.m_lineStyle: str = LineStyleEnum.SOLID.optionValue + self.m_lineWidth: float = 1.0 + self.m_markerStyle: str = MarkerStyleEnum.NONE.optionValue + self.m_markerSize: float = 1.0 + + # user choices + self.m_userChoices: dict[str, Any] = { + "variableName": "", + "curveNames": [], + "curveConvention": [], + "inputNames": [], + "plotRegions": False, + "reverseXY": False, + "logScaleX": False, + "logScaleY": False, + "minorticks": False, + "displayTitle": True, + "title": "title1", + "titleStyle": FontStyleEnum.NORMAL.optionValue, + "titleWeight": FontWeightEnum.BOLD.optionValue, + "titleSize": 12, + "legendDisplay": True, + "legendPosition": LegendLocationEnum.BEST.optionValue, + "legendSize": 10, + "removeJobName": True, + "removeRegions": False, + "curvesAspect": {}, + } + + def getUserChoices(self: Self) -> dict[str, Any]: + """Access the m_userChoices attribute. + + Returns: + dict[str] : the user choices for the figure. + """ + return self.m_userChoices + + def getInputNames(self: Self) -> set[str]: + """Get source names from user selection. + + Returns: + set[str] : source names from ParaView pipeline. + """ + inputAvailables = self.a01GetInputSources() + inputNames: set[str] = set(pvt.getArrayChoices(inputAvailables)) + return inputNames + + def defineInputNames(self: Self) -> None: + """Adds the input names to the userChoices.""" + inputNames: set[str] = self.getInputNames() + self.m_userChoices["inputNames"] = inputNames + + def defineUserChoicesCurves(self: Self) -> None: + """Define user choices for curves to plot.""" + sourceNames: set[str] = self.getInputNames() + dasPlot = self.b02GetCurvesToPlot() + dasMinus1 = self.b07GetCurveConvention() + curveNames: set[str] = set(pvt.getArrayChoices(dasPlot)) + minus1Names: set[str] = set(pvt.getArrayChoices(dasMinus1)) + toUse1: set[str] = pvt.integrateSourceNames(sourceNames, curveNames) + toUse2: set[str] = pvt.integrateSourceNames(sourceNames, minus1Names) + self.m_userChoices["curveNames"] = tuple(toUse1) + self.m_userChoices["curveConvention"] = tuple(toUse2) + + def defineCurvesAspect(self: Self) -> None: + """Define user choices for curve aspect properties.""" + curveAspect: tuple[tuple[float, float, float], str, float, str, float] = ( + self.getCurveAspect() + ) + curveName: str = self.getCurveToUse() + self.m_userChoices["curvesAspect"][curveName] = curveAspect + + def buildPythonViewScript(self: Self) -> str: + """Builds the Python script used to launch the Python View. + + The script is returned as a string to be then injected in the Python + View. + + Returns: + str: Complete Python View script. + """ + sourceNames: set[str] = self.getInputNames() + userChoices: dict[str, Any] = self.getUserChoices() + script: str = f"timestep = '{str(GetActiveView().ViewTime)}'\n" + script += f"sourceNames = {sourceNames}\n" + script += f"variableName = '{userChoices['variableName']}'\n" + script += f"dir_path = '{dir_path}'\n" + script += f"userChoices = {userChoices}\n\n\n" + with open(self.m_pathPythonViewScript) as file: + fileContents = file.read() + script += fileContents + return script + + def buildNewLayoutWithPythonView(self: Self) -> None: + """Create a new Python View layout.""" + # we first built the new layout + layout_names: list[str] = self.m_organizationDisplay.getLayoutsNames() + nb_layouts: int = len(layout_names) + # imagine two layouts already exists, the new one will be named "Layout #3" + layoutName: str = "Layout #" + str(nb_layouts + 1) + # check that we that the layoutName is new and does not belong to the list of layout_names, + # if not we modify the layoutName until it is a new one + if layoutName in layout_names: + cpt: int = 2 + while layoutName in layout_names: + layoutName = "Layout #" + str(nb_layouts + cpt) + cpt += 1 + self.m_organizationDisplay.addLayout(layoutName) + self.m_layoutName = layoutName + + # we then build the new python view + self.m_organizationDisplay.addViewToLayout("PythonView", layoutName, 0) + self.m_pythonView = self.m_organizationDisplay.getLayoutViews()[layoutName][0] + Show(GetActiveSource(), self.m_pythonView, "PythonRepresentation") + + # widgets definition + """The names of the @smproperty methods command names below have a letter in lower case in + front because PARAVIEW displays properties in the alphabetical order. + See https://gitlab.kitware.com/paraview/paraview/-/issues/21493 for possible improvements on + this issue""" + + @smproperty.dataarrayselection(name="InputSources") + def a01GetInputSources(self: Self) -> vtkDataArraySelection: + """Get all valid sources for the filter. + + Returns: + vtkDataArraySelection: valid data sources. + """ + return self.m_validSources + + @smproperty.xml( + """ + + """ + ) + def a02GroupFlow(self: Self) -> None: + """Organize groups.""" + self.Modified() + + @smproperty.stringvector(name="CurvesAvailable", information_only="1") + def b00GetCurvesAvailable(self: Self) -> list[str]: + """Get the available curves. + + Returns: + list[str]: list of curves. + """ + return self.m_validColumnsDataframe + + @smproperty.stringvector(name="Abscissa", number_of_elements="1") + @smdomain.xml( + """ + + """ + ) + def b01SetVariableName(self: Self, name: str) -> None: + """Set the name of X axis variable. + + Args: + name: name of the variable. + """ + self.m_userChoices["variableName"] = name + self.Modified() + + @smproperty.dataarrayselection(name="Ordinate") + def b02GetCurvesToPlot(self: Self) -> vtkDataArraySelection: + """Get the curves to plot. + + Returns: + vtkDataArraySelection: data to plot. + """ + return self.m_curvesToPlot + + @smproperty.intvector( + name="PlotsPerRegion", label="PlotsPerRegion", default_values=0 + ) + @smdomain.xml("""""") + def b03SetPlotsPerRegion(self: Self, boolean: bool) -> None: + """Set plot per region option. + + Args: + boolean: user choice. + """ + self.m_userChoices["plotRegions"] = boolean + self.Modified() + + @smproperty.xml( + """ + + + + """ + ) + def b04GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector( + name="CurveConvention", + label="Select Curves To Change Convention", + default_values=0, + ) + @smdomain.xml("""""") + def b05SetCurveConvention(self: Self, boolean: bool) -> None: + """Select Curves To Change Convention. + + Args: + boolean: user choice. + """ + self.m_multiplyCurves = boolean + + @smproperty.xml( + """ + + """ + ) + def b06GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.dataarrayselection(name="CurveConventionSelection") + def b07GetCurveConvention(self: Self) -> vtkDataArraySelection: + """Get the curves to change convention. + + Returns: + vtkDataArraySelection: selected curves to change convention. + """ + return self.m_curvesMinus1 + + @smproperty.xml( + """ + + + """ + ) + def b08GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector( + name="EditAxisProperties", label="Edit Axis Properties", default_values=0 + ) + @smdomain.xml("""""") + def c01SetEditAxisProperties(self: Self, boolean: bool) -> None: + """Set option to edit axis properties. + + Args: + boolean (bool): user choice. + """ + self.Modified() + + @smproperty.xml( + """ + + """ + ) + def c02GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector(name="ReverseXY", label="Reverse XY Axes", default_values=0) + @smdomain.xml("""""") + def c02SetReverseXY(self: Self, boolean: bool) -> None: + """Set option to reverse X and Y axes. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["reverseXY"] = boolean + self.Modified() + + @smproperty.intvector(name="LogScaleX", label="X Axis Log Scale", default_values=0) + @smdomain.xml("""""") + def c03SetReverseXY(self: Self, boolean: bool) -> None: + """Set option to log scale for X axis. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["logScaleX"] = boolean + self.Modified() + + @smproperty.intvector(name="LogScaleY", label="Y Axis Log Scale", default_values=0) + @smdomain.xml("""""") + def c04SetReverseXY(self: Self, boolean: bool) -> None: + """Set option to log scale for Y axis. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["logScaleY"] = boolean + self.Modified() + + @smproperty.intvector( + name="Minorticks", label="Display Minor ticks", default_values=0 + ) + @smdomain.xml("""""") + def c05SetMinorticks(self: Self, boolean: bool) -> None: + """Set option to display minor ticks. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["minorticks"] = boolean + self.Modified() + + @smproperty.intvector( + name="CustomAxisLim", label="Use Custom Axis Limits", default_values=0 + ) + @smdomain.xml("""""") + def c06SetCustomAxisLim(self: Self, boolean: bool) -> None: + """Set option to define axis limits. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["customAxisLim"] = boolean + self.Modified() + + @smproperty.doublevector(name="LimMinX", label="X min", default_values=-1e36) + def c07LimMinX(self: Self, value: float) -> None: + """Set X axis min. + + Args: + value (float): X axis min. + """ + value2: Union[float, None] = value + if value2 == -1e36: + value2 = None + self.m_userChoices["limMinX"] = value2 + self.Modified() + + @smproperty.doublevector(name="LimMaxX", label="X max", default_values=1e36) + def c08LimMaxX(self: Self, value: float) -> None: + """Set X axis max. + + Args: + value (float): X axis max. + """ + value2: Union[float, None] = value + if value2 == 1e36: + value2 = None + self.m_userChoices["limMaxX"] = value2 + self.Modified() + + @smproperty.doublevector(name="LimMinY", label="Y min", default_values=-1e36) + def c09LimMinY(self: Self, value: float) -> None: + """Set Y axis min. + + Args: + value (float): Y axis min. + """ + value2: Union[float, None] = value + if value2 == -1e36: + value2 = None + self.m_userChoices["limMinY"] = value2 + self.Modified() + + @smproperty.doublevector(name="LimMaxY", label="Y max", default_values=1e36) + def c10LimMaxY(self: Self, value: float) -> None: + """Set Y axis max. + + Args: + value (float): Y axis max. + """ + value2: Union[float, None] = value + if value2 == 1e36: + value2 = None + self.m_userChoices["limMaxY"] = value2 + self.Modified() + + @smproperty.xml( + """ + + + + + + """ + ) + def c11GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.xml( + """ + + + + + + + """ + ) + def c12GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector(name="DisplayTitle", label="Display Title", default_values=1) + @smdomain.xml("""""") + def d01SetDisplayTitle(self: Self, boolean: bool) -> None: + """Set option to display title. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["displayTitle"] = boolean + self.Modified() + + @smproperty.xml( + """ + + """ + ) + def d02GroupFlow(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.stringvector(name="Title", default_values="title1") + def d03SetTitlePlot(self: Self, title: str) -> None: + """Set title. + + Args: + title (str): title. + """ + self.m_userChoices["title"] = title + self.Modified() + + @smproperty.intvector(name="TitleStyle", label="Title Style", default_values=0) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, FontStyleEnum))) + def d04SetTitleStyle(self: Self, value: int) -> None: + """Set title font style. + + Args: + value (int): title font style index in FontStyleEnum. + """ + choice = list(FontStyleEnum)[value] + self.m_userChoices["titleStyle"] = choice.optionValue + self.Modified() + + @smproperty.intvector(name="TitleWeight", label="Title Weight", default_values=1) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, FontWeightEnum))) + def d05SetTitleWeight(self: Self, value: int) -> None: + """Set title font weight. + + Args: + value (int): title font weight index in FontWeightEnum. + """ + choice = list(FontWeightEnum)[value] + self.m_userChoices["titleWeight"] = choice.optionValue + self.Modified() + + @smproperty.intvector(name="TitleSize", label="Title Size", default_values=12) + @smdomain.xml("""""") + def d06SetTitleSize(self: Self, size: float) -> None: + """Set title font size. + + Args: + size (float): title font size between 1 and 50. + """ + self.m_userChoices["titleSize"] = size + self.Modified() + + @smproperty.xml( + """ + panel_visibility="advanced"> + + + + + + """ + ) + def d07PropertyGroup(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector( + name="DisplayLegend", label="Display Legend", default_values=1 + ) + @smdomain.xml("""""") + def e00SetDisplayLegend(self: Self, boolean: bool) -> None: + """Set option to display legend. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["displayLegend"] = boolean + self.Modified() + + @smproperty.xml( + """ + + """ + ) + def e01PropertyGroup(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector( + name="LegendPosition", label="Legend Position", default_values=0 + ) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, LegendLocationEnum))) + def e02SetLegendPosition(self: Self, value: int) -> None: + """Set legend position. + + Args: + value (int): legend position index in LegendLocationEnum. + """ + choice = list(LegendLocationEnum)[value] + self.m_userChoices["legendPosition"] = choice.optionValue + self.Modified() + + @smproperty.intvector(name="LegendSize", label="Legend Size", default_values=10) + @smdomain.xml("""""") + def e03SetLegendSize(self: Self, size: float) -> None: + """Set legend font size. + + Args: + size (float): legend font size between 1 and 50. + """ + self.m_userChoices["legendSize"] = size + self.Modified() + + @smproperty.intvector( + name="RemoveJobName", label="Remove Job Name in legend", default_values=1 + ) + @smdomain.xml("""""") + def e04SetRemoveJobName(self: Self, boolean: bool) -> None: + """Set option to remove job names from legend. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["removeJobName"] = boolean + self.Modified() + + @smproperty.intvector( + name="RemoveRegionsName", + label="Remove Regions Name in legend", + default_values=0, + ) + @smdomain.xml("""""") + def e05SetRemoveRegionsName(self: Self, boolean: bool) -> None: + """Set option to remove region names from legend. + + Args: + boolean (bool): user choice. + """ + self.m_userChoices["removeRegions"] = boolean + self.Modified() + + @smproperty.xml( + """ + + + + + + """ + ) + def e06PropertyGroup(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.intvector( + name="ModifyCurvesAspect", label="Edit Curve Graphics", default_values=1 + ) + @smdomain.xml("""""") + def f01SetModifyCurvesAspect(self: Self, boolean: bool) -> None: + """Set option to change curve aspects. + + Args: + boolean (bool): user choice. + """ + self.m_modifyCurvesAspect = boolean + + @smproperty.xml( + """ + + """ + ) + def f02PropertyGroup(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.stringvector(name="CurvesInfo", information_only="1") + def f03GetCurveNames(self: Self) -> list[str]: + """Get curves to modify aspects. + + Returns: + set[str]: curves to modify aspects. + """ + return list(self.m_curvesToModify) + + # TODO: still usefull? + @smproperty.stringvector(name="CurveToModify", number_of_elements="1") + @smdomain.xml( + """ + + """ + ) + def f04SetCircleID(self: Self, value: str) -> None: + """Set m_curveToUse. + + Args: + value (float): value of m_curveToUse + """ + self.m_curveToUse = value + self.Modified() + + def getCurveToUse(self: Self) -> str: + """Get m_curveToUse.""" + return self.m_curveToUse + + @smproperty.intvector(name="LineStyle", label="Line Style", default_values=1) + @smdomain.xml(optionEnumToXml(cast(OptionSelectionEnum, LineStyleEnum))) + def f05SetLineStyle(self: Self, value: int) -> None: + """Set line style. + + Args: + value (int): line style index in LineStyleEnum + """ + choice = list(LineStyleEnum)[value] + self.m_lineStyle = choice.optionValue + self.Modified() + + @smproperty.doublevector(name="LineWidth", default_values=1.0) + @smdomain.xml("""""") + def f06SetLineWidth(self: Self, value: float) -> None: + """Set line width. + + Args: + value (float): line width between 1 and 10. + """ + self.m_lineWidth = value + self.Modified() + + @smproperty.intvector(name="MarkerStyle", label="Marker Style", default_values=0) + @smdomain.xml(optionEnumToXml(cast(LegendLocationEnum, MarkerStyleEnum))) + def f07SetMarkerStyle(self: Self, value: int) -> None: + """Set marker style. + + Args: + value (int): Marker style index in MarkerStyleEnum + """ + choice = list(MarkerStyleEnum)[value] + self.m_markerStyle = choice.optionValue + self.Modified() + + @smproperty.doublevector(name="MarkerSize", default_values=1.0) + @smdomain.xml("""""") + def f08SetMarkerSize(self: Self, value: float) -> None: + """Set marker size. + + Args: + value (float): size of markers between 1 and 30. + """ + self.m_markerSize = value + self.Modified() + + @smproperty.xml( + """ + + + + + + + + """ + ) + def f09PropertyGroup(self: Self) -> None: + """Organized groups.""" + self.Modified() + + @smproperty.doublevector( + name="ColorEnvelop", default_values=[0, 0, 0], number_of_elements=3 + ) + @smdomain.xml("""""") + def f10SetColor(self: Self, value0: float, value1: float, value2: float) -> None: + """Set envelope color. + + Args: + value0 (float): Red color between 0 and 1. + + value1 (float): Green color between 0 and 1. + + value2 (float): Blue color between 0 and 1. + """ + self.m_color = (value0, value1, value2) + self.Modified() + + @smproperty.xml( + """ + + + """ + ) + def f11PropertyGroup(self: Self) -> None: + """Organized groups.""" + self.Modified() + + def getCurveAspect( + self: Self, + ) -> tuple[tuple[float, float, float], str, float, str, float]: + """Get curve aspect properties according to user choices. + + Returns: + tuple: (color, linestyle, linewidth, marker, markersize) + """ + return ( + self.m_color, + self.m_lineStyle, + self.m_lineWidth, + self.m_markerStyle, + self.m_markerSize, + ) + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkDataObject") + else: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkDataObject") + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, # noqa: F841 + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + # pythonViewGeneration + assert self.m_pythonView is not None, "No Python View was found." + viewSize = GetActiveView().ViewSize + self.m_userChoices["ratio"] = viewSize[0] / viewSize[1] + self.defineInputNames() + self.defineUserChoicesCurves() + self.defineCurvesAspect() + self.m_pythonView.Script = self.buildPythonViewScript() + Render() + return 1 diff --git a/geos-posp/src/PVplugins/PVSurfaceGeomechanics.py b/geos-posp/src/PVplugins/PVSurfaceGeomechanics.py new file mode 100644 index 00000000..b789e900 --- /dev/null +++ b/geos-posp/src/PVplugins/PVSurfaceGeomechanics.py @@ -0,0 +1,262 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +import numpy as np +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkDataObject, + vtkMultiBlockDataSet, + vtkPolyData, +) + +from geos_posp.filters.SurfaceGeomechanics import SurfaceGeomechanics +from geos_posp.processing.multiblockInpectorTreeFunctions import ( + getBlockElementIndexesFlatten, + getBlockFromFlatIndex, +) +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_DEG, + DEFAULT_ROCK_COHESION, +) + +__doc__ = r""" +PVSurfaceGeomechanics is a Paraview plugin that allows to compute +additional geomechanical attributes from the input surfaces. + +Input and output types are vtkMultiBlockDataSet. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVSurfaceGeomechanics. +* Select any pipeline child of the second ouput from + GeosExtractMergeBlocksVolumeSurface* filter. +* Search and Apply PVSurfaceGeomechanics Filter. + +""" + + +@smproxy.filter(name="PVSurfaceGeomechanics", label="Geos Surface Geomechanics") +@smhint.xml('') +@smproperty.input(name="Input", port_index=0) +@smdomain.datatype(dataTypes=["vtkMultiBlockDataSet"], composite_data_supported=True) +class PVSurfaceGeomechanics(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to compute additional geomechanical surface outputs. + + Input is either a vtkMultiBlockDataSet that contains surfaces with + Normals and Tangential attributes. + """ + super().__init__( + nInputPorts=1, + nOutputPorts=1, + inputType="vtkMultiBlockDataSet", + outputType="vtkMultiBlockDataSet", + ) + + # rock cohesion (Pa) + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + # friction angle (°) + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_DEG + # logger + self.m_logger: Logger = getLogger("Surface Geomechanics Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + @smproperty.doublevector( + name="RockCohesion", + label="Rock Cohesion (Pa)", + default_values=DEFAULT_ROCK_COHESION, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference rock cohesion to compute critical pore pressure. + The unit is Pa. Default is fractured case (i.e., 0. Pa). + + """ + ) + def a01SetRockCohesion(self: Self, value: float) -> None: + """Set rock cohesion. + + Args: + value (float): rock cohesion (Pa) + """ + self.m_rockCohesion = value + self.Modified() + + def getRockCohesion(self: Self) -> float: + """Get rock cohesion. + + Returns: + float: rock cohesion. + """ + return self.m_rockCohesion + + @smproperty.doublevector( + name="FrictionAngle", + label="Friction Angle (°)", + default_values=DEFAULT_FRICTION_ANGLE_DEG, + panel_visibility="default", + ) + @smdomain.xml( + """ + + Reference friction angle to compute critical pore pressure. + The unit is °. Default is no friction case (i.e., 0.°). + + """ + ) + def a02SetFrictionAngle(self: Self, value: float) -> None: + """Set frition angle. + + Args: + value (float): friction angle (°) + """ + self.m_frictionAngle = value + self.Modified() + + def getFrictionAngle(self: Self) -> float: + """Get friction angle in radian. + + Returns: + float: friction angle. + """ + return self.m_frictionAngle * np.pi / 180.0 + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + + self.m_logger.info(f"Apply filter {__name__}") + try: + input0: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + output: vtkMultiBlockDataSet = self.GetOutputData(outInfoVec, 0) + + assert input0 is not None, "Input Surface is null." + assert output is not None, "Output pipeline is null." + + output.ShallowCopy(input0) + self.computeSurfaceGeomecanics(input0, output) + output.Modified() + mess: str = ( + "Surface geomechanics attributes calculation successfully ended." + ) + self.m_logger.info(mess) + except AssertionError as e: + mess1: str = "Surface geomechanics attributes calculation failed due to:" + self.m_logger.error(mess1) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Surface geomechanics attributes calculation failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def computeSurfaceGeomecanics( + self: Self, input: vtkMultiBlockDataSet, output: vtkMultiBlockDataSet + ) -> None: + """Compute surface geomechanics new attributes. + + Args: + input (vtkMultiBlockDataSet): input multiBlockDataSet + output (vtkMultiBlockDataSet): output multiBlockDataSet + """ + + surfaceBlockIndexes: list[int] = getBlockElementIndexesFlatten(input) + for blockIndex in surfaceBlockIndexes: + surfaceBlock0: vtkDataObject = getBlockFromFlatIndex(output, blockIndex) + assert surfaceBlock0 is not None, "Surface is undefined." + surfaceBlock: vtkPolyData = vtkPolyData.SafeDownCast(surfaceBlock0) + filter: SurfaceGeomechanics = SurfaceGeomechanics() + filter.AddInputDataObject(surfaceBlock) + filter.SetRockCohesion(self.getRockCohesion()) + filter.SetFrictionAngle(self.getFrictionAngle()) + filter.Update() + outputSurface: vtkPolyData = filter.GetOutputDataObject(0) + + # add attributes to output surface mesh + for attributeName in filter.GetNewAttributeNames(): + attr: vtkDataArray = outputSurface.GetCellData().GetArray(attributeName) + surfaceBlock.GetCellData().AddArray(attr) + surfaceBlock.GetCellData().Modified() + surfaceBlock.Modified() + output.Modified() diff --git a/geos-posp/src/PVplugins/PVTransferAttributesVolumeSurface.py b/geos-posp/src/PVplugins/PVTransferAttributesVolumeSurface.py new file mode 100644 index 00000000..9ecd7a15 --- /dev/null +++ b/geos-posp/src/PVplugins/PVTransferAttributesVolumeSurface.py @@ -0,0 +1,293 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys + +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.dirname(dir_path) +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from paraview.simple import ( # type: ignore[import-not-found] + FindSource, + GetActiveSource, + GetSources, + servermanager, +) +from paraview.util.vtkAlgorithm import ( # type: ignore[import-not-found] + VTKPythonAlgorithmBase, + smdomain, + smhint, + smproperty, + smproxy, +) +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonCore import ( + vtkDataArraySelection as vtkDAS, +) +from vtkmodules.vtkCommonDataModel import ( + vtkDataObject, + vtkMultiBlockDataSet, + vtkPolyData, + vtkUnstructuredGrid, +) + +from geos_posp.filters.TransferAttributesVolumeSurface import ( + TransferAttributesVolumeSurface, +) +from geos_posp.processing.multiblockInpectorTreeFunctions import ( + getBlockElementIndexesFlatten, + getBlockFromFlatIndex, +) +from geos_posp.processing.vtkUtils import getAttributeSet, mergeBlocks +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.visu.PVUtils.checkboxFunction import ( # type: ignore[attr-defined] + createModifiedCallback, +) +from geos_posp.visu.PVUtils.paraviewTreatments import getArrayChoices + +__doc__ = """ +PVTransferAttributesVolumeSurface is a Paraview plugin that allows to map face ids from +surface mesh with cell ids from volume mesh. + +Input and output types are vtkMultiBlockDataSet. + +To use it: + +* Load the module in Paraview: Tools>Manage Plugins...>Load new>PVTransferAttributesVolumeSurface. +* Select first a volume mesh, then a surface mesh, both of type vtkMultiBlockDataSet +* Search and Apply 'Geos Volume Surface Mesh Mapper' Filter. + +""" + + +@smproxy.filter( + name="PVTransferAttributesVolumeSurface", + label="Geos Transfer Attributes From Volume to Surface", +) +@smhint.xml('') +@smproperty.input(name="SurfaceMesh", port_index=1) +@smdomain.datatype( + dataTypes=["vtkMultiBlockDataSet", "vtkUnstructuredGrid", "vtkPolyData"], + composite_data_supported=True, +) +@smproperty.input(name="VolumeMesh", port_index=0) +@smdomain.datatype( + dataTypes=["vtkMultiBlockDataSet", "vtkUnstructuredGrid"], + composite_data_supported=True, +) +class PVTransferAttributesVolumeSurface(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Paraview plugin to compute additional geomechanical surface outputs. + + Input is either a vtkMultiBlockDataSet that contains surfaces with + Normals and Tangential attributes. + """ + super().__init__( + nInputPorts=2, nOutputPorts=1, outputType="vtkMultiBlockDataSet" + ) + + #: input volume mesh + self.m_volumeMesh: vtkMultiBlockDataSet + #: output surface mesh + self.m_outputSurfaceMesh: vtkMultiBlockDataSet + # volume mesh source + self.m_sourceNameVolume: str = [ + k for (k, v) in GetSources().items() if v == GetActiveSource() + ][0][0] + + # list of attributes + self.m_attributes: vtkDAS = self.createAttributeVTKDas() + # logger + self.m_logger: Logger = getLogger("Volume Surface Mesh Mapper Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def createAttributeVTKDas(self: Self) -> vtkDAS: + """Create the vtkDataArraySelection with cell attribute names. + + Returns: + vtkDAS: vtkDataArraySelection with attribute names + """ + source = FindSource(self.m_sourceNameVolume) + dataset = servermanager.Fetch(source) + attributes: set[str] = getAttributeSet(dataset, False) + attributesDAS: vtkDAS = vtkDAS() + for attribute in attributes: + attributesDAS.AddArray(attribute, False) + attributesDAS.AddObserver("ModifiedEvent", createModifiedCallback(self)) # type: ignore[arg-type] + return attributesDAS + + @smproperty.dataarrayselection(name="AttributesToTransfer") + def a02GetAttributeToTransfer(self: Self) -> vtkDAS: + """Get selected attribute names to transfer. + + Returns: + vtkDataArraySelection: selected attribute names. + """ + return self.m_attributes + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + else: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData1 = self.GetInputData(inInfoVec, 0, 0) + inData2 = self.GetInputData(inInfoVec, 1, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData1 is not None + assert inData2 is not None + if outData is None or (not outData.IsA(inData2.GetClassName())): + outData = inData2.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + self.m_logger.info(f"Apply filter {__name__}") + self.SetProgressText("Computation in progress...") + self.SetProgressShiftScale(50, 100) + + self.m_volumeMesh = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + surfaceMesh: vtkMultiBlockDataSet = vtkMultiBlockDataSet.GetData( + inInfoVec[1] + ) + self.m_outputSurfaceMesh = self.GetOutputData(outInfoVec, 0) + + assert self.m_volumeMesh is not None, "Input Volume mesh is null." + assert surfaceMesh is not None, "Input Surface mesh is null." + assert self.m_outputSurfaceMesh is not None, "Output pipeline is null." + + self.m_outputSurfaceMesh.ShallowCopy(surfaceMesh) + self.transferAttributes() + + self.m_logger.info("Attributes were successfully transfered.") + except AssertionError as e: + mess: str = "Attribute transfer failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Attribute transfer failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def transferAttributes(self: Self) -> bool: + """Do transfer attributes from volume to surface. + + Returns: + bool: True if transfer is successfull, False otherwise. + """ + + attributeNames: set[str] = set( + getArrayChoices(self.a02GetAttributeToTransfer()) + ) + volumeMeshMerged: vtkUnstructuredGrid = mergeBlocks(self.m_volumeMesh) + surfaceBlockIndexes: list[int] = getBlockElementIndexesFlatten( + self.m_outputSurfaceMesh + ) + for blockIndex in surfaceBlockIndexes: + surfaceBlock0: vtkDataObject = getBlockFromFlatIndex( + self.m_outputSurfaceMesh, blockIndex + ) + assert surfaceBlock0 is not None, "surfaceBlock0 is undefined." + surfaceBlock: vtkPolyData = vtkPolyData.SafeDownCast(surfaceBlock0) + assert surfaceBlock is not None, "surfaceBlock is undefined." + + assert isinstance(surfaceBlock, vtkPolyData), "Wrong object type." + + # do transfer of attributes + filter: TransferAttributesVolumeSurface = TransferAttributesVolumeSurface() + filter.AddInputDataObject(0, volumeMeshMerged) + filter.AddInputDataObject(1, surfaceBlock) + filter.SetAttributeNamesToTransfer(attributeNames) + filter.Update() + outputSurface: vtkUnstructuredGrid = filter.GetOutputDataObject(0) + + # add attributes to output surface mesh + for attributeName in filter.GetNewAttributeNames(): + attr: vtkDataArray = outputSurface.GetCellData().GetArray(attributeName) + surfaceBlock.GetCellData().AddArray(attr) + surfaceBlock.GetCellData().Modified() + surfaceBlock.Modified() + + self.m_outputSurfaceMesh.Modified() + return True diff --git a/geos-posp/src/PVplugins/__init__.py b/geos-posp/src/PVplugins/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/PVplugins/py.typed b/geos-posp/src/PVplugins/py.typed new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/__init__.py b/geos-posp/src/geos_posp/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/filters/AttributeMappingFromCellCoords.py b/geos-posp/src/geos_posp/filters/AttributeMappingFromCellCoords.py new file mode 100644 index 00000000..a8933765 --- /dev/null +++ b/geos-posp/src/geos_posp/filters/AttributeMappingFromCellCoords.py @@ -0,0 +1,249 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Raphaël Vinour, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file + +from collections.abc import MutableSequence + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkDoubleArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCellData, + vtkCellLocator, + vtkUnstructuredGrid, +) + +from geos_posp.processing.vtkUtils import ( + computeCellCenterCoordinates, + createEmptyAttribute, + getVtkArrayInObject, +) +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +AttributeMappingFromCellCoords module is a vtk filter that map two identical mesh (or a mesh is +an extract from the other one) and create an attribute containing shared cell ids. + +Filter input and output types are vtkUnstructuredGrid. + +To use the filter: + +.. code-block:: python + + from filters.AttributeMappingFromCellCoords import AttributeMappingFromCellCoords + + # filter inputs + logger :Logger + input :vtkUnstructuredGrid + TransferAttributeName : str + + # instanciate the filter + filter :AttributeMappingFromCellCoords = AttributeMappingFromCellCoords() + # set the logger + filter.SetLogger(logger) + # set input data object + filter.SetInputDataObject(input) + # set Attribute to transfer + filter.SetTransferAttributeNames(AttributeName) + # set Attribute to compare + filter.SetIDAttributeName(AttributeName) + # do calculations + filter.Update() + # get output object + output :vtkPolyData = filter.GetOutputDataObject(0) + # get created attribute names + newAttributeNames :set[str] = filter.GetNewAttributeNames() +""" + + +class AttributeMappingFromCellCoords(VTKPythonAlgorithmBase): + + def __init__(self: Self) -> None: + """Map the properties of a source mesh to a receiver mesh.""" + super().__init__( + nInputPorts=2, nOutputPorts=1, outputType="vtkUnstructuredGrid" + ) + + # source mesh + self.m_clientMesh: vtkUnstructuredGrid + # input mesh + self.m_serverMesh: vtkUnstructuredGrid + # cell map + self.m_cellMap: npt.NDArray[np.int64] = np.empty(0).astype(int) + + # Transfer Attribute name + self.m_transferedAttributeNames: set[str] = set() + # logger + self.m_logger: Logger = getLogger("Attribute Mapping From Cell Coords Filter") + + def SetTransferAttributeNames( + self: Self, transferredAttributeNames: set[str] + ) -> None: + """Setter for transferredAttributeName. + + Args: + transferredAttributeNames (set[str]): set of names of the + attributes to transfer. + + """ + self.m_transferedAttributeNames.clear() + for name in transferredAttributeNames: + self.m_transferedAttributeNames.add(name) + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + self.Modified() + + def GetCellMap(self: Self) -> npt.NDArray[np.int64]: + """Getter of cell map.""" + return self.m_cellMap + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + + try: + self.m_serverMesh = vtkUnstructuredGrid.GetData(inInfoVec[0]) + clientMesh = vtkUnstructuredGrid.GetData(inInfoVec[1]) + self.m_clientMesh = self.GetOutputData(outInfoVec, 0) + + assert self.m_serverMesh is not None, "Server mesh is null." + assert clientMesh is not None, "Client mesh is null." + assert self.m_clientMesh is not None, "Output pipeline is null." + + self.m_clientMesh.ShallowCopy(clientMesh) + + # create cell map + self.computeCellMapping() + + # transfer attributes if at least one corresponding cell + if np.any(self.m_cellMap > -1): + self.transferAttributes() + self.m_clientMesh.Modified() + else: + self.m_logger.warning( + "Input and output meshes do not have any corresponding cells" + ) + + except AssertionError as e: + mess1: str = "Mapping Transfer Coord failed due to:" + self.m_logger.error(mess1) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Mapping Transfer Coord failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + mess2: str = "Mapping Transfer Coord were successfully computed." + self.m_logger.info(mess2) + + return 1 + + def computeCellMapping(self: Self) -> bool: + """Create the cell map from client to server mesh cell indexes. + + For each cell index of the client mesh, stores the index of the cell + in the server mesh. + + Returns: + bool: True if the map was computed. + + """ + self.m_cellMap = np.full(self.m_clientMesh.GetNumberOfCells(), -1).astype(int) + cellLocator: vtkCellLocator = vtkCellLocator() + cellLocator.SetDataSet(self.m_serverMesh) + cellLocator.BuildLocator() + + cellCenters: vtkDataArray = computeCellCenterCoordinates(self.m_clientMesh) + for i in range(self.m_clientMesh.GetNumberOfCells()): + cellCoords: MutableSequence[float] = [0.0, 0.0, 0.0] + cellCenters.GetTuple(i, cellCoords) + cellIndex: int = cellLocator.FindCell(cellCoords) + self.m_cellMap[i] = cellIndex + return True + + def transferAttributes(self: Self) -> bool: + """Transfer attributes from server to client meshes using cell mapping. + + Returns: + bool: True if transfer successfully ended. + + """ + for attributeName in self.m_transferedAttributeNames: + array: vtkDoubleArray = getVtkArrayInObject( + self.m_serverMesh, attributeName, False + ) + + dataType = array.GetDataType() + nbComponents: int = array.GetNumberOfComponents() + componentNames: list[str] = [] + if nbComponents > 1: + for i in range(nbComponents): + componentNames.append(array.GetComponentName(i)) + newArray: vtkDataArray = createEmptyAttribute( + self.m_clientMesh, attributeName, tuple(componentNames), dataType, False + ) + nanValues: list[float] = [np.nan for _ in range(nbComponents)] + for indexClient in range(self.m_clientMesh.GetNumberOfCells()): + indexServer: int = self.m_cellMap[indexClient] + data: MutableSequence[float] = nanValues + if indexServer > -1: + array.GetTuple(indexServer, data) + newArray.InsertNextTuple(data) + + cellData: vtkCellData = self.m_clientMesh.GetCellData() + assert cellData is not None, "CellData is undefined." + cellData.AddArray(newArray) + cellData.Modified() + return True diff --git a/geos-posp/src/geos_posp/filters/AttributeMappingFromCellId.py b/geos-posp/src/geos_posp/filters/AttributeMappingFromCellId.py new file mode 100644 index 00000000..6e28bb3f --- /dev/null +++ b/geos-posp/src/geos_posp/filters/AttributeMappingFromCellId.py @@ -0,0 +1,200 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Raphaël Vinour, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import numpy as np +import numpy.typing as npt +from typing_extensions import Self +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkUnstructuredGrid + +from geos_posp.processing.vtkUtils import createAttribute, getArrayInObject +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +AttributeMappingFromCellId module is a vtk filter that transfer a attribute from a +server mesh to a client mesh. + +Filter input and output types are vtkPolyData. + +To use the filter: + +.. code-block:: python + + from filters.AttributeMappingFromCellId import AttributeMappingFromCellId + + # filter inputs + logger :Logger + input :vtkPolyData + TransferAttributeName : str + + # instanciate the filter + filter :AttributeMappingFromCellId = AttributeMappingFromCellId() + # set the logger + filter.SetLogger(logger) + # set input data object + filter.SetInputDataObject(input) + # set Attribute to transfer + filter.SetTransferAttributeName(AttributeName) + # set Attribute to compare + filter.SetIDAttributeName(AttributeName) + # do calculations + filter.Update() + # get output object + output :vtkPolyData = filter.GetOutputDataObject(0) + # get created attribute names + newAttributeNames :set[str] = filter.GetNewAttributeNames() +""" + + +class AttributeMappingFromCellId(VTKPythonAlgorithmBase): + + def __init__(self: Self) -> None: + """Map the properties of a source mesh to a receiver mesh.""" + super().__init__( + nInputPorts=2, nOutputPorts=1, outputType="vtkUnstructuredGrid" + ) + + # Transfer Attribute name + self.m_transferedAttributeName: str = "" + # ID Attribute name + self.m_idAttributeName: str = "" + # logger + self.m_logger: Logger = getLogger("Attribute Mapping From Cell Id Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set filter logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + self.Modified() + + def SetTransferAttributeName(self: Self, name: str) -> None: + """Set Transfer attribute name.""" + self.m_transferedAttributeName = name + self.Modified() + + def SetIDAttributeName(self: Self, name: str) -> None: + """Set ID attribute name.""" + self.m_idAttributeName = name + self.Modified() + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + + try: + serverMesh: vtkUnstructuredGrid = vtkUnstructuredGrid.GetData(inInfoVec[0]) + clientMesh: vtkUnstructuredGrid = vtkUnstructuredGrid.GetData(inInfoVec[1]) + outData: vtkUnstructuredGrid = self.GetOutputData(outInfoVec, 0) + + assert serverMesh is not None, "Server mesh is null." + assert clientMesh is not None, "Client mesh is null." + assert outData is not None, "Output pipeline is null." + + outData.ShallowCopy(clientMesh) + + cellIdMap: npt.NDArray[np.int64] = self.getCellMap(serverMesh, clientMesh) + + attributeArrayServer: npt.NDArray[np.float64] = getArrayInObject( + serverMesh, self.m_transferedAttributeName, False + ) + attributeArrayClient: npt.NDArray[np.float64] = np.full_like( + attributeArrayServer, np.nan + ) + for i in range(serverMesh.GetNumberOfCells()): + k: int = cellIdMap[i] + attributeArrayClient[k] = attributeArrayServer[i] + createAttribute( + clientMesh, + attributeArrayClient, + self.m_transferedAttributeName, + (), + False, + ) + outData.Modified() + + except AssertionError as e: + mess1: str = "Attribute mapping failed due to:" + self.m_logger.error(mess1) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Attribute mapping failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + mess2: str = ( + f"Attribute {self.m_transferedAttributeName} was successfully transferred." + ) + self.m_logger.info(mess2) + + return 1 + + def getCellMap( + self: Self, serverMesh: vtkUnstructuredGrid, clientMesh: vtkUnstructuredGrid + ) -> npt.NDArray[np.int64]: + """Compute the mapping between both mesh from cell ids. + + Args: + serverMesh (vtkUnstructuredGrid): server mesh + clientMesh (vtkUnstructuredGrid): client mesh + + Returns: + npt.NDArray[np.int64]: the map where for each cell index of the + client mesh, the cell index of the server mesh. + + """ + cellIdArrayServer: npt.NDArray[np.int64] = getArrayInObject( + serverMesh, self.m_idAttributeName, False + ).astype(int) + cellIdArrayClient: npt.NDArray[np.int64] = getArrayInObject( + clientMesh, self.m_idAttributeName, False + ).astype(int) + cellMap: npt.NDArray[np.int64] = np.zeros(serverMesh.GetNumberOfCells()).astype( + int + ) + for i, cellId in enumerate(cellIdArrayServer): + k: int = np.argwhere(cellIdArrayClient == cellId)[0] + cellMap[i] = k + return cellMap diff --git a/geos-posp/src/geos_posp/filters/GeomechanicsCalculator.py b/geos-posp/src/geos_posp/filters/GeomechanicsCalculator.py new file mode 100644 index 00000000..0f8e9ba1 --- /dev/null +++ b/geos-posp/src/geos_posp/filters/GeomechanicsCalculator.py @@ -0,0 +1,1747 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +from typing import Union + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import ( + vtkDataSet, + vtkPointSet, + vtkUnstructuredGrid, +) +from vtkmodules.vtkFiltersCore import vtkCellCenters + +import geos_posp.processing.geomechanicsCalculatorFunctions as fcts +from geos_posp.processing.vtkUtils import ( + createAttribute, + getArrayInObject, + getComponentNames, + isAttributeInObject, +) +from geos_posp.utils.GeosOutputsConstants import ( + AttributeEnum, + ComponentNameEnum, + GeosMeshOutputsEnum, + PostProcessingOutputsEnum, +) +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_GRAIN_BULK_MODULUS, + DEFAULT_ROCK_COHESION, + GRAVITY, + WATER_DENSITY, +) + +__doc__ = """ +GeomechanicsCalculator module is a vtk filter that allows to compute additional +Geomechanical properties from existing ones. + +GeomechanicsCalculator filter inputs are either vtkPointSet or vtkUnstructuredGrid +and returned object is of same type as input. + +To use the filter: + +.. code-block:: python + + import numpy as np + from filters.GeomechanicsCalculator import GeomechanicsCalculator + + # filter inputs + logger :Logger + # input object + input :Union[vtkPointSet, vtkUnstructuredGrid] + # grain bulk modulus in Pa (e.g., use a very high value to get a Biot coefficient equal to 1) + grainBulkModulus :float = 1e26 + # Reference density to compute specific gravity (e.g. fresh water density) in kg.m^-3 + specificDensity :float = 1000. + # rock cohesion in Pa + rockCohesion :float = 1e8 + # friction angle in ° + frictionAngle :float = 10 * np.pi / 180. + + # instanciate the filter + geomechanicsCalculatorFilter :GeomechanicsCalculator = GeomechanicsCalculator() + + # set filter attributes + # set logger + geomechanicsCalculatorFilter.SetLogger(logger) + # set input object + geomechanicsCalculatorFilter.SetInputDataObject(input) + # set computeAdvancedOutputsOn or computeAdvancedOutputsOff to compute or + # not advanced outputs... + geomechanicsCalculatorFilter.computeAdvancedOutputsOn() + # set oter parameters + geomechanicsCalculatorFilter.SetGrainBulkModulus(grainBulkModulus) + geomechanicsCalculatorFilter.SetSpecificDensity(specificDensity) + # rock cohesion and friction angle are used for advanced outputs only + geomechanicsCalculatorFilter.SetRockCohesion(rockCohesion) + geomechanicsCalculatorFilter.SetFrictionAngle(frictionAngle) + # do calculations + geomechanicsCalculatorFilter.Update() + # get filter output (same type as input) + output :Union[vtkPointSet, vtkUnstructuredGrid] = geomechanicsCalculatorFilter.GetOutputDataObject(0) +""" + +TYPE_ERROR_MESSAGE = ( + "Input object must by either a vtkPointSet or a vtkUntructuredGrid." +) +UNDEFINED_ATTRIBUTE_MESSAGE = " attribute is undefined." + + +class GeomechanicsCalculator(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """VTK Filter to perform Geomechanical output computation. + + Input object is either a vtkPointSet or a vtkUntructuredGrid. + """ + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkDataSet") # type: ignore[no-untyped-call] + + self.m_output: Union[vtkPointSet, vtkUnstructuredGrid] + + # additional parameters + self.m_computeAdvancedOutputs: bool = False + self.m_grainBulkModulus: float = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity: float = WATER_DENSITY + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + + # computation results + self.m_elasticModuliComputed: bool = False + self.m_biotCoefficientComputed: bool = False + self.m_compressibilityComputed: bool = False + self.m_effectiveStressComputed: bool = False + self.m_totalStressComputed: bool = False + self.m_effectiveStressRatioOedComputed: bool = False + + # will compute resuls if m_ready is True (updated by initFilter method) + self.m_ready: bool = False + # attributes are either on points or on cells + self.m_attributeOnPoints: bool = False + # elastic moduli are either bulk and Shear moduli (m_computeYoungPoisson=True) + # or young Modulus and poisson's ratio (m_computeYoungPoisson=False) + self.m_computeYoungPoisson: bool = True + + # set m_logger + self.m_logger: Logger = getLogger("Geomechanics calculator") + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) # type: ignore[no-untyped-call] + outData = self.GetOutputData(outInfoVec, 0) # type: ignore[no-untyped-call] + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input: vtkDataSet = vtkDataSet.GetData(inInfoVec[0]) + assert input is not None, "Input object is null." + + # initialize output objects + self.m_output = self.GetOutputData(outInfoVec, 0) # type: ignore[no-untyped-call] + assert self.m_output is not None, "Output object is null." + self.m_output.ShallowCopy(input) + + # check the input and update self.m_ready, m_attributeOnPoints and m_computeBulkAndShear + self.initFilter() + if not self.m_ready: + mess: str = ( + "Mandatory properties are missing to compute geomechanical outputs:" + ) + mess += ( + f"Either {PostProcessingOutputsEnum.YOUNG_MODULUS.attributeName} " + f"and {PostProcessingOutputsEnum.POISSON_RATIO.attributeName} or " + f"{GeosMeshOutputsEnum.BULK_MODULUS.attributeName} and " + f"{GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName} must be " + f"present in the data as well as the " + f"{GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName} attribute." + ) + self.m_logger.error(mess) + return 0 + + self.computeBasicOutputs() + if self.m_computeAdvancedOutputs: + self.computeAdvancedOutputs() + + except AssertionError as e: + mess1: str = "Geomechanical attribute calculation failed due to:" + self.m_logger.error(mess1) + self.m_logger.error(str(e)) + return 0 + except Exception as e: + mess2: str = "Geomechanical attribut calculation failed due to:" + self.m_logger.critical(mess2) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def SetLogger(self: Self, logger: Logger) -> None: + """Set the logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + self.Modified() + + def computeAdvancedOutputsOn(self: Self) -> None: + """Activate advanced outputs calculation.""" + self.m_computeAdvancedOutputs = True + self.Modified() + + def computeAdvancedOutputsOff(self: Self) -> None: + """Deactivate advanced outputs calculation.""" + self.m_computeAdvancedOutputs = False + self.Modified() + + def SetGrainBulkModulus(self: Self, grainBulkModulus: float) -> None: + """Set the grain bulk modulus. + + Args: + grainBulkModulus (float): grain bulk modulus + """ + self.m_grainBulkModulus = grainBulkModulus + self.Modified() + + def SetSpecificDensity(self: Self, specificDensity: float) -> None: + """Set the specific density. + + Args: + specificDensity (float): pecific density + """ + self.m_specificDensity = specificDensity + self.Modified() + + def SetRockCohesion(self: Self, rockCohesion: float) -> None: + """Set the rock cohesion. + + Args: + rockCohesion (float): rock cohesion + """ + self.m_rockCohesion = rockCohesion + self.Modified() + + def SetFrictionAngle(self: Self, frictionAngle: float) -> None: + """Set the friction angle. + + Args: + frictionAngle (float): friction angle (rad) + """ + self.m_frictionAngle = frictionAngle + self.Modified() + + def getOutputType(self: Self) -> str: + """Get output object type. + + Returns: + str: type of output object. + """ + output: vtkDataSet = self.GetOutputDataObject(0) + assert output is not None, "Output is null." + return output.GetClassName() + + def resetDefaultValues(self: Self) -> None: + """Reset filter parameters to the default values.""" + self.m_computeAdvancedOutputs = False + self.m_grainBulkModulus = DEFAULT_GRAIN_BULK_MODULUS + self.m_specificDensity = WATER_DENSITY + self.m_rockCohesion = DEFAULT_ROCK_COHESION + self.m_frictionAngle = DEFAULT_FRICTION_ANGLE_RAD + + self.m_elasticModuliComputed = False + self.m_biotCoefficientComputed = False + self.m_compressibilityComputed = False + self.m_effectiveStressComputed = False + self.m_totalStressComputed = False + self.m_effectiveStressRatioOedComputed = False + self.m_ready = False + self.Modified() + + def initFilter(self: Self) -> None: + """Check that mandatory attributes are present in the data set. + + Determine if attributes are on cells or on Points. + Set self.m_ready = True if all data is ok, False otherwise + """ + # check attributes are on cells, or on points otherwise + attributeOnPoints: bool = False + attributeOnCells: bool = self.checkMandatoryAttributes(False) + if not attributeOnCells: + attributeOnPoints = self.checkMandatoryAttributes(True) + + self.m_ready = attributeOnPoints or attributeOnCells + self.m_attributeOnPoints = attributeOnPoints + + def checkMandatoryAttributes(self: Self, onPoints: bool) -> bool: + """Check that mandatory attributes are present in the mesh. + + The mesh must contains either the young Modulus and Poisson's ratio + (m_computeYoungPoisson=False) or the bulk and shear moduli + (m_computeYoungPoisson=True) + + Args: + onPoints (bool): attributes are on points (True) or on cells (False) + + Returns: + bool: True if all needed attributes are present, False otherwise + """ + youngModulusAttributeName: str = ( + PostProcessingOutputsEnum.YOUNG_MODULUS.attributeName + ) + poissonRatioAttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO.attributeName + ) + bulkModulusAttributeName: str = GeosMeshOutputsEnum.BULK_MODULUS.attributeName + shearModulusAttributeName: str = GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName + effectiveStressAttributeName: str = ( + GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName + ) + + self.m_computeYoungPoisson = not isAttributeInObject( + self.m_output, youngModulusAttributeName, onPoints + ) or not isAttributeInObject(self.m_output, poissonRatioAttributeName, onPoints) + + # if none of elastic moduli is present, return False + if self.m_computeYoungPoisson and ( + not isAttributeInObject(self.m_output, bulkModulusAttributeName, onPoints) + or not isAttributeInObject( + self.m_output, shearModulusAttributeName, onPoints + ) + ): + return False + + # check effective Stress is present + ret: bool = isAttributeInObject( + self.m_output, effectiveStressAttributeName, onPoints + ) + return ret + + def computeBasicOutputs(self: Self) -> bool: + """Compute basic geomechanical outputs. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + if not self.m_ready: + return False + + try: + self.m_elasticModuliComputed = self.computeElasticModulus() + if not self.m_elasticModuliComputed: + mess: str = ( + "Geomechanical outputs cannot be computed without elastic moduli." + ) + self.m_logger.error(mess) + return False + + self.m_biotCoefficientComputed = self.computeBiotCoefficient() + if not self.m_biotCoefficientComputed: + mess2: str = ( + "Total stress, elastic strain, and advanced geomechanical " + + "outputs cannot be computed without Biot coefficient." + ) + self.m_logger.warning(mess2) + + self.m_compressibilityComputed = self.computeCompressibilityCoefficient() + + self.m_effectiveStressComputed = self.computeRealEffectiveStressRatio() + if not self.m_effectiveStressComputed: + mess3: str = ( + "Total stress, elastic strain, and advanced geomechanical " + + "outputs cannot be computed without effective stress." + ) + self.m_logger.warning(mess3) + + specificGravityComputed: bool = self.computeSpecificGravity() + + # TODO: deactivate lithostatic stress calculation until right formula + litostaticStressComputed: bool = True # self.computeLitostaticStress() + + elasticStrainComputed: bool = False + if self.m_effectiveStressComputed: + if self.m_biotCoefficientComputed: + self.m_totalStressComputed = self.computeTotalStresses() + if self.m_elasticModuliComputed: + elasticStrainComputed = self.computeElasticStrain() + + reservoirStressPathOedComputed: bool = False + if self.m_elasticModuliComputed: + # oedometric DRSP (effective stress ratio in oedometric conditions) + self.m_effectiveStressRatioOedComputed = ( + self.computeEffectiveStressRatioOed() + ) + + if self.m_biotCoefficientComputed: + reservoirStressPathOedComputed = ( + self.computeReservoirStressPathOed() + ) + + reservoirStressPathRealComputed: bool = False + if self.m_totalStressComputed: + reservoirStressPathRealComputed = self.computeReservoirStressPathReal() + + if ( + self.m_elasticModuliComputed + and self.m_biotCoefficientComputed + and self.m_compressibilityComputed + and self.m_effectiveStressComputed + and specificGravityComputed + and elasticStrainComputed + and litostaticStressComputed + and self.m_totalStressComputed + and self.m_effectiveStressRatioOedComputed + and reservoirStressPathRealComputed + and reservoirStressPathRealComputed + and reservoirStressPathOedComputed + and reservoirStressPathRealComputed + ): + mess4: str = ( + "All geomechanical basic outputs were successfully computed." + ) + self.m_logger.info(mess4) + else: + mess5: str = "Some geomechanical basic outputs were not computed." + self.m_logger.warning(mess5) + + except AssertionError as e: + mess6: str = ( + "Some of the geomechanical basic outputs were " + "not computed due to:" + ) + self.m_logger.error(mess6) + self.m_logger.error(str(e)) + return False + except Exception as e: + mess7: str = ( + "Some of the geomechanical basic outputs were " + "not computed due to:" + ) + self.m_logger.critical(mess7) + self.m_logger.critical(e, exc_info=True) + return False + return True + + def computeAdvancedOutputs(self: Self) -> bool: + """Compute advanced geomechanical outputs. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + if not self.m_ready: + return False + + try: + fractureIndexesComputed: bool = False + criticalPorePressure: bool = False + if self.m_totalStressComputed: + fractureIndexesComputed = self.computeCriticalTotalStressRatio() + criticalPorePressure = self.computeCriticalPorePressure() + + if ( + self.m_effectiveStressRatioOedComputed + and fractureIndexesComputed + and criticalPorePressure + ): + mess: str = ( + "All geomechanical advanced outputs were " + + "successfully computed." + ) + self.m_logger.info(mess) + else: + mess0: str = ( + "Some geomechanical advanced outputs were " + "not computed." + ) + self.m_logger.warning(mess0) + + except AssertionError as e: + mess1: str = ( + "Some of the geomechanical basic outputs were " + "not computed due to:" + ) + self.m_logger.error(mess1) + self.m_logger.error(str(e)) + return False + except Exception as e: + mess2: str = ( + "Some of the geomechanical advanced outputs " + + "were not computed due to:" + ) + self.m_logger.critical(mess2) + self.m_logger.critical(e, exc_info=True) + return False + return True + + def computeElasticModulus(self: Self) -> bool: + """Compute elastic moduli. + + Young modulus and the poisson ratio computed from shear and bulk moduli + if needed. + + Returns: + bool: True if elastic moduli are already present or if calculation + successfully ended, False otherwise. + """ + if self.m_computeYoungPoisson: + return self.computeElasticModulusFromBulkShear() + return self.computeElasticModulusFromYoungPoisson() + + def computeElasticModulusFromBulkShear(self: Self) -> bool: + """Compute Young modulus Poisson's ratio from bulk and shear moduli. + + Returns: + bool: True if calculation successfully ended, False otherwise + """ + youngModulusAttributeName: str = ( + PostProcessingOutputsEnum.YOUNG_MODULUS.attributeName + ) + poissonRatioAttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO.attributeName + ) + bulkModulusAttributeName: str = GeosMeshOutputsEnum.BULK_MODULUS.attributeName + shearModulusAttributeName: str = GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName + + ret: bool = True + bulkModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, bulkModulusAttributeName, self.m_attributeOnPoints + ) + + shearModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, shearModulusAttributeName, self.m_attributeOnPoints + ) + try: + assert bulkModulus is not None, ( + f"{bulkModulusAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert shearModulus is not None, ( + f"{shearModulusAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + except AssertionError as e: + self.m_logger.error("Elastic moduli were not computed due to:") + self.m_logger.error(str(e)) + return False + + try: + youngModulus: npt.NDArray[np.float64] = fcts.youngModulus( + bulkModulus, shearModulus + ) + # assert np.any(youngModulus < 0), ("Young modulus yields negative " + + # "values. Check Bulk and Shear modulus values.") + createAttribute( + self.m_output, + youngModulus, + youngModulusAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Young modulus was not computed due to:") + self.m_logger.error(str(e)) + ret = False + + try: + poissonRatio: npt.NDArray[np.float64] = fcts.poissonRatio( + bulkModulus, shearModulus + ) + # assert np.any(poissonRatio < 0), ("Poisson ratio yields negative " + + # "values. Check Bulk and Shear modulus values.") + createAttribute( + self.m_output, + poissonRatio, + poissonRatioAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Poisson's ratio was not computed due to:") + self.m_logger.error(str(e)) + ret = False + + return ret + + def computeElasticModulusFromYoungPoisson(self: Self) -> bool: + """Compute bulk modulus from Young Modulus and Poisson's ratio. + + Returns: + bool: True if bulk modulus was wuccessfully computed, False otherwise + """ + try: + youngModulusAttributeName: str = ( + PostProcessingOutputsEnum.YOUNG_MODULUS.attributeName + ) + poissonRatioAttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO.attributeName + ) + bulkModulusAttributeName: str = ( + GeosMeshOutputsEnum.BULK_MODULUS.attributeName + ) + if not isAttributeInObject( + self.m_output, bulkModulusAttributeName, self.m_attributeOnPoints + ): + youngModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, youngModulusAttributeName, self.m_attributeOnPoints + ) + poissonRatio: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, poissonRatioAttributeName, self.m_attributeOnPoints + ) + + assert youngModulus is not None, ( + f"{youngModulusAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert poissonRatio is not None, ( + f"{poissonRatioAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + bulkModulus: npt.NDArray[np.float64] = fcts.bulkModulus( + youngModulus, poissonRatio + ) + # assert np.any(bulkModulus < 0), ("Bulk modulus yields negative " + + # "values. Check Young modulus and Poisson ratio values.") + ret: bool = createAttribute( + self.m_output, + bulkModulus, + bulkModulusAttributeName, + (), + self.m_attributeOnPoints, + ) + return ret + + except AssertionError as e: + self.m_logger.error("Bulk modulus was not computed due to:") + self.m_logger.error(str(e)) + return False + return True + + def computeBiotCoefficient(self: Self) -> bool: + """Compute Biot coefficient from default and grain bulk modulus. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + biotCoefficientAttributeName: str = ( + PostProcessingOutputsEnum.BIOT_COEFFICIENT.attributeName + ) + if not isAttributeInObject( + self.m_output, biotCoefficientAttributeName, self.m_attributeOnPoints + ): + bulkModulusAttributeName: str = ( + GeosMeshOutputsEnum.BULK_MODULUS.attributeName + ) + bulkModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, bulkModulusAttributeName, self.m_attributeOnPoints + ) + try: + assert bulkModulus is not None, ( + f"{bulkModulusAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + biotCoefficient: npt.NDArray[np.float64] = fcts.biotCoefficient( + self.m_grainBulkModulus, bulkModulus + ) + createAttribute( + self.m_output, + biotCoefficient, + biotCoefficientAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Biot coefficient was not computed due to:") + self.m_logger.error(str(e)) + return False + + return True + + def computeCompressibilityCoefficient(self: Self) -> bool: + """Compute compressibility coefficient from simulation outputs. + + Compressibility coefficient is computed from Poisson's ratio, bulk + modulus, Biot coefficient and Porosity. + + Returns: + bool: True if the attribute is correctly created, False otherwise. + """ + compressibilityAttributeName: str = ( + PostProcessingOutputsEnum.COMPRESSIBILITY.attributeName + ) + bulkModulusAttributeName: str = GeosMeshOutputsEnum.BULK_MODULUS.attributeName + bulkModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, bulkModulusAttributeName, self.m_attributeOnPoints + ) + porosityAttributeName: str = GeosMeshOutputsEnum.POROSITY.attributeName + porosity: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, porosityAttributeName, self.m_attributeOnPoints + ) + porosityInitialAttributeName: str = ( + GeosMeshOutputsEnum.POROSITY_INI.attributeName + ) + porosityInitial: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, porosityInitialAttributeName, self.m_attributeOnPoints + ) + if not isAttributeInObject( + self.m_output, compressibilityAttributeName, self.m_attributeOnPoints + ): + poissonRatioAttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO.attributeName + ) + poissonRatio: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, poissonRatioAttributeName, self.m_attributeOnPoints + ) + biotCoefficientAttributeName: str = ( + PostProcessingOutputsEnum.BIOT_COEFFICIENT.attributeName + ) + biotCoefficient: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, biotCoefficientAttributeName, self.m_attributeOnPoints + ) + + try: + assert poissonRatio is not None, ( + f"{poissonRatioAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert bulkModulus is not None, ( + f"{bulkModulusAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert biotCoefficient is not None, ( + f"{biotCoefficientAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert porosity is not None, ( + f"{porosityAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + compressibility: npt.NDArray[np.float64] = fcts.compressibility( + poissonRatio, bulkModulus, biotCoefficient, porosity + ) + createAttribute( + self.m_output, + compressibility, + compressibilityAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Compressibility was not computed due to:") + self.m_logger.error(str(e)) + return False + + # oedometric compressibility + compressibilityOedAttributeName: str = ( + PostProcessingOutputsEnum.COMPRESSIBILITY_OED.attributeName + ) + if not isAttributeInObject( + self.m_output, compressibilityOedAttributeName, self.m_attributeOnPoints + ): + shearModulusAttributeName: str = ( + GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName + ) + shearModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, shearModulusAttributeName, self.m_attributeOnPoints + ) + try: + assert poissonRatio is not None, ( + f"{poissonRatioAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert bulkModulus is not None, ( + f"{bulkModulusAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert porosityInitial is not None, ( + f"{porosityInitialAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + compressibilityOed: npt.NDArray[np.float64] = fcts.compressibilityOed( + bulkModulus, shearModulus, porosityInitial + ) + createAttribute( + self.m_output, + compressibilityOed, + compressibilityOedAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error( + "Oedometric Compressibility was not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + # real compressibility + compressibilityRealAttributeName: str = ( + PostProcessingOutputsEnum.COMPRESSIBILITY_REAL.attributeName + ) + if not isAttributeInObject( + self.m_output, compressibilityRealAttributeName, self.m_attributeOnPoints + ): + deltaPressureAttributeName: str = ( + GeosMeshOutputsEnum.DELTA_PRESSURE.attributeName + ) + deltaPressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, deltaPressureAttributeName, self.m_attributeOnPoints + ) + try: + assert deltaPressure is not None, ( + f"{deltaPressureAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert porosityInitial is not None, ( + f"{porosityInitialAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert porosity is not None, ( + f"{porosityAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + compressibilityReal: npt.NDArray[np.float64] = fcts.compressibilityReal( + deltaPressure, porosity, porosityInitial + ) + createAttribute( + self.m_output, + compressibilityReal, + compressibilityRealAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Real compressibility was not computed due to:") + self.m_logger.error(str(e)) + return False + + return True + + def computeSpecificGravity(self: Self) -> bool: + """Create Specific gravity attribute. + + Specific gravity is computed from rock density attribute and specific + density input. + + Returns: + bool: True if the attribute is correctly created, False otherwise. + """ + densityAttributeName: str = GeosMeshOutputsEnum.ROCK_DENSITY.attributeName + density: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, densityAttributeName, self.m_attributeOnPoints + ) + specificGravityAttributeName: str = ( + PostProcessingOutputsEnum.SPECIFIC_GRAVITY.attributeName + ) + if not isAttributeInObject( + self.m_output, specificGravityAttributeName, self.m_attributeOnPoints + ): + try: + assert density is not None, ( + f"{densityAttributeName} " + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + specificGravity: npt.NDArray[np.float64] = fcts.specificGravity( + density, self.m_specificDensity + ) + createAttribute( + self.m_output, + specificGravity, + specificGravityAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Specific gravity was not computed due to:") + self.m_logger.error(str(e)) + return False + + return True + + def computeRealEffectiveStressRatio(self: Self) -> bool: + """Compute effective stress ratio. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + # test if effective stress is in the table + if not isAttributeInObject( + self.m_output, + GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName, + self.m_attributeOnPoints, + ): + self.m_logger.error("Effective stress is not in input data.") + return False + + # real effective stress ratio + return self.computeStressRatioReal( + GeosMeshOutputsEnum.STRESS_EFFECTIVE, + PostProcessingOutputsEnum.STRESS_EFFECTIVE_RATIO_REAL, + ) + + def computeTotalStresses(self: Self) -> bool: + """Compute total stress total stress ratio. + + Total stress is computed at the initial and current time steps. + total stress ratio is computed at current time step only. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + # compute total stress at initial time step + totalStressT0AttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL_INITIAL.attributeName + ) + if not isAttributeInObject( + self.m_output, totalStressT0AttributeName, self.m_attributeOnPoints + ): + self.computeTotalStressInitial() + + # compute total stress at current time step + totalStressAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL.attributeName + ) + if not isAttributeInObject( + self.m_output, totalStressAttributeName, self.m_attributeOnPoints + ): + try: + effectiveStressAttributeName: str = ( + GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName + ) + effectiveStress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, + effectiveStressAttributeName, + self.m_attributeOnPoints, + ) + assert effectiveStress is not None, ( + f"{effectiveStressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + pressureAttributeName: str = GeosMeshOutputsEnum.PRESSURE.attributeName + pressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, pressureAttributeName, self.m_attributeOnPoints + ) + assert pressure is not None, ( + f"{pressureAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + biotCoefficientAttributeName: str = ( + PostProcessingOutputsEnum.BIOT_COEFFICIENT.attributeName + ) + biotCoefficient: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, + biotCoefficientAttributeName, + self.m_attributeOnPoints, + ) + assert biotCoefficient is not None, ( + f"{biotCoefficientAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + self.doComputeTotalStress( + effectiveStress, pressure, biotCoefficient, totalStressAttributeName + ) + self.computeStressRatioReal( + PostProcessingOutputsEnum.STRESS_TOTAL, + PostProcessingOutputsEnum.STRESS_TOTAL_RATIO_REAL, + ) + + except AssertionError as e: + self.m_logger.error( + "Total stress at current time step was not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + return True + + def computeTotalStressInitial(self: Self) -> bool: + """Compute total stress at initial time step. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + try: + + # compute elastic moduli at initial time step + bulkModulusT0: npt.NDArray[np.float64] + + bulkModulusT0AttributeName: str = ( + PostProcessingOutputsEnum.BULK_MODULUS_INITIAL.attributeName + ) + youngModulusT0AttributeName: str = ( + PostProcessingOutputsEnum.YOUNG_MODULUS_INITIAL.attributeName + ) + poissonRatioT0AttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO_INITIAL.attributeName + ) + # get bulk modulus at initial time step + if isAttributeInObject( + self.m_output, bulkModulusT0AttributeName, self.m_attributeOnPoints + ): + + bulkModulusT0 = getArrayInObject( + self.m_output, bulkModulusT0AttributeName, self.m_attributeOnPoints + ) + # or compute it from Young and Poisson if not an attribute + elif isAttributeInObject( + self.m_output, youngModulusT0AttributeName, self.m_attributeOnPoints + ) and isAttributeInObject( + self.m_output, poissonRatioT0AttributeName, self.m_attributeOnPoints + ): + + youngModulusT0: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, youngModulusT0AttributeName, self.m_attributeOnPoints + ) + poissonRatioT0: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, poissonRatioT0AttributeName, self.m_attributeOnPoints + ) + assert poissonRatioT0 is not None, "Poisson's ratio is undefined." + assert youngModulusT0 is not None, "Young modulus is undefined." + bulkModulusT0 = fcts.bulkModulus(youngModulusT0, poissonRatioT0) + else: + raise AssertionError("Elastic moduli at initial time are absent.") + + assert ( + bulkModulusT0 is not None + ), "Bulk modulus at initial time step is undefined." + + # compute Biot at initial time step + biotCoefficientT0: npt.NDArray[np.float64] = fcts.biotCoefficient( + self.m_grainBulkModulus, bulkModulusT0 + ) + assert ( + biotCoefficientT0 is not None + ), "Biot coefficient at initial time step is undefined." + + # compute total stress at initial time step + # get effective stress attribute + effectiveStressAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_EFFECTIVE_INITIAL.attributeName + ) + effectiveStress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, effectiveStressAttributeName, self.m_attributeOnPoints + ) + assert effectiveStress is not None, ( + f"{effectiveStressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + # get pressure attribute + pressureAttributeName: str = GeosMeshOutputsEnum.PRESSURE.attributeName + pressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, pressureAttributeName, self.m_attributeOnPoints + ) + pressureT0: npt.NDArray[np.float64] + # case pressureT0 is None, total stress = effective stress + # (managed by doComputeTotalStress function) + if pressure is not None: + # get delta pressure to recompute pressure at initial time step (pressureTo) + deltaPressureAttributeName: str = ( + GeosMeshOutputsEnum.DELTA_PRESSURE.attributeName + ) + deltaPressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, deltaPressureAttributeName, self.m_attributeOnPoints + ) + assert deltaPressure is not None, ( + f"{deltaPressureAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + pressureT0 = pressure - deltaPressure + + totalStressT0AttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL_INITIAL.attributeName + ) + return self.doComputeTotalStress( + effectiveStress, + pressureT0, + biotCoefficientT0, + totalStressT0AttributeName, + ) + + except AssertionError as e: + self.m_logger.error( + "Total stress at initial time step was not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + def doComputeTotalStress( + self: Self, + effectiveStress: npt.NDArray[np.float64], + pressure: Union[npt.NDArray[np.float64], None], + biotCoefficient: npt.NDArray[np.float64], + totalStressAttributeName: str, + ) -> bool: + """Compute total stress from effective stress and pressure. + + Args: + effectiveStress (npt.NDArray[np.float64]): effective stress + pressure (npt.NDArray[np.float64] | None): pressure + biotCoefficient (npt.NDArray[np.float64]): biot coefficient + totalStressAttributeName (str): total stress attribute name + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + totalStress: npt.NDArray[np.float64] + # if pressure data is missing, total stress equals effective stress + if pressure is None: + # copy effective stress data + totalStress = np.copy(effectiveStress) + mess: str = ( + "Pressure attribute is undefined, " + + "total stress will be equal to effective stress." + ) + self.m_logger.warning(mess) + else: + if np.isnan(pressure).any(): + mess0: str = ( + "Some cells do not have pressure data, " + + "total stress will be equal to effective stress." + ) + self.m_logger.warning(mess0) + + # replace nan values by 0. + pressure[np.isnan(pressure)] = 0.0 + totalStress = fcts.totalStress(effectiveStress, biotCoefficient, pressure) + + # create total stress attribute + assert totalStress is not None, "Total stress data is null." + createAttribute( + self.m_output, + totalStress, + totalStressAttributeName, + ComponentNameEnum.XYZ.value, + self.m_attributeOnPoints, + ) + return True + + def computeLitostaticStress(self: Self) -> bool: + """Compute lithostatic stress. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + litostaticStressAttributeName: str = ( + PostProcessingOutputsEnum.LITHOSTATIC_STRESS.attributeName + ) + if not isAttributeInObject( + self.m_output, litostaticStressAttributeName, self.m_attributeOnPoints + ): + + densityAttributeName: str = GeosMeshOutputsEnum.ROCK_DENSITY.attributeName + density: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, densityAttributeName, self.m_attributeOnPoints + ) + try: + depth: npt.NDArray[np.float64] + if self.m_attributeOnPoints: + depth = self.computeDepthAlongLine() + else: + depth = self.computeDepthInMesh() + + assert depth is not None, "Depth is undefined." + assert density is not None, ( + f"{densityAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + litostaticStress = fcts.lithostaticStress(depth, density, GRAVITY) + createAttribute( + self.m_output, + litostaticStress, + litostaticStressAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Lithostatic stress was not computed due to:") + self.m_logger.error(str(e)) + return False + + return True + + def computeDepthAlongLine(self: Self) -> npt.NDArray[np.float64]: + """Compute depth along a line. + + Returns: + npt.NDArray[np.float64]: 1D array with depth property + """ + # get z coordinate + zCoord: npt.NDArray[np.float64] = self.getZcoordinates() + assert zCoord is not None, "Depth coordinates cannot be computed." + + # TODO: to find how to compute depth in a general case + # GEOS z axis is upward + depth: npt.NDArray[np.float64] = -1.0 * zCoord + return depth + + def computeDepthInMesh(self: Self) -> npt.NDArray[np.float64]: + """Compute depth of each cell in a mesh. + + Returns: + npt.NDArray[np.float64]: array with depth property + """ + # get z coordinate + zCoord: npt.NDArray[np.float64] = self.getZcoordinates() + assert zCoord is not None, "Depth coordinates cannot be computed." + + # TODO: to find how to compute depth in a general case + depth: npt.NDArray[np.float64] = -1.0 * zCoord + return depth + + def getZcoordinates(self: Self) -> npt.NDArray[np.float64]: + """Get z coordinates from self.m_output. + + Returns: + npt.NDArray[np.float64]: 1D array with depth property + """ + # get z coordinate + zCoord: npt.NDArray[np.float64] + pointCoords: npt.NDArray[np.float64] = self.getPointCoordinates() + assert pointCoords is not None, "Point coordinates are undefined." + assert pointCoords.shape[1] == 2, "Point coordinates are undefined." + zCoord = pointCoords[:, 2] + return zCoord + + def computeElasticStrain(self: Self) -> bool: + """Compute elastic strain from effective stress and elastic modulus. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + elasticStrainAttributeName: str = ( + PostProcessingOutputsEnum.STRAIN_ELASTIC.attributeName + ) + if not isAttributeInObject( + self.m_output, elasticStrainAttributeName, self.m_attributeOnPoints + ): + effectiveStressAttributeName: str = ( + GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName + ) + effectiveStress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, effectiveStressAttributeName, self.m_attributeOnPoints + ) + + effectiveStressIniAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_EFFECTIVE_INITIAL.attributeName + ) + effectiveStressIni: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, effectiveStressIniAttributeName, self.m_attributeOnPoints + ) + + bulkModulusAttributeName: str = ( + GeosMeshOutputsEnum.BULK_MODULUS.attributeName + ) + bulkModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, bulkModulusAttributeName, self.m_attributeOnPoints + ) + + shearModulusAttributeName: str = ( + GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName + ) + shearModulus: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, shearModulusAttributeName, self.m_attributeOnPoints + ) + + try: + assert effectiveStress is not None, ( + f"{effectiveStressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert effectiveStressIni is not None, ( + f"{effectiveStressIniAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert bulkModulus is not None, ( + f"{bulkModulusAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert shearModulus is not None, ( + f"{shearModulusAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + deltaEffectiveStress = effectiveStress - effectiveStressIni + elasticStrain: npt.NDArray[np.float64] = ( + fcts.elasticStrainFromBulkShear( + deltaEffectiveStress, bulkModulus, shearModulus + ) + ) + createAttribute( + self.m_output, + elasticStrain, + elasticStrainAttributeName, + ComponentNameEnum.XYZ.value, + self.m_attributeOnPoints, + ) + + except AssertionError as e: + self.m_logger.error("Elastic strain was not computed due to:") + self.m_logger.error(str(e)) + return False + return True + + def computeReservoirStressPathReal(self: Self) -> bool: + """Compute reservoir stress paths. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + RSPrealAttributeName: str = PostProcessingOutputsEnum.RSP_REAL.attributeName + if not isAttributeInObject( + self.m_output, RSPrealAttributeName, self.m_attributeOnPoints + ): + # real RSP + try: + # total stress at current and initial time steps + totalStressAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL.attributeName + ) + totalStress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, totalStressAttributeName, self.m_attributeOnPoints + ) + + totalStressT0AttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL_INITIAL.attributeName + ) + totalStressIni: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, totalStressT0AttributeName, self.m_attributeOnPoints + ) + + deltaPressureAttributeName: str = ( + GeosMeshOutputsEnum.DELTA_PRESSURE.attributeName + ) + deltaPressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, deltaPressureAttributeName, self.m_attributeOnPoints + ) + + assert totalStress is not None, ( + f"{totalStressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert totalStressIni is not None, ( + f"{totalStressT0AttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert deltaPressure is not None, ( + f"{deltaPressureAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + # create delta stress attribute for QC + deltaTotalStressAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL_DELTA.attributeName + ) + deltaStress: npt.NDArray[np.float64] = totalStress - totalStressIni + componentNames: tuple[str, ...] = getComponentNames( + self.m_output, totalStressAttributeName, self.m_attributeOnPoints + ) + assert deltaStress is not None, ( + f"{deltaTotalStressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + createAttribute( + self.m_output, + deltaStress, + deltaTotalStressAttributeName, + componentNames, + self.m_attributeOnPoints, + ) + + RSPreal: npt.NDArray[np.float64] = fcts.reservoirStressPathReal( + deltaStress, deltaPressure + ) + assert RSPreal is not None, ( + f"{RSPrealAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + createAttribute( + self.m_output, + RSPreal, + RSPrealAttributeName, + componentNames, + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error( + "Reservoir stress path in real conditions was " + + "not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + return True + + def computeReservoirStressPathOed(self: Self) -> bool: + """Compute Reservoir Stress Path in oedometric conditions. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + RSPOedAttributeName: str = PostProcessingOutputsEnum.RSP_OED.attributeName + if not isAttributeInObject( + self.m_output, RSPOedAttributeName, self.m_attributeOnPoints + ): + + poissonRatioAttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO.attributeName + ) + poissonRatio: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, poissonRatioAttributeName, self.m_attributeOnPoints + ) + + biotCoefficientAttributeName: str = ( + PostProcessingOutputsEnum.BIOT_COEFFICIENT.attributeName + ) + biotCoefficient: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, biotCoefficientAttributeName, self.m_attributeOnPoints + ) + + try: + assert poissonRatio is not None, ( + f"{poissonRatioAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert biotCoefficient is not None, ( + f"{biotCoefficientAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + RSPoed: npt.NDArray[np.float64] = fcts.reservoirStressPathOed( + biotCoefficient, poissonRatio + ) + createAttribute( + self.m_output, + RSPoed, + RSPOedAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Oedometric RSP was not computed due to:") + self.m_logger.error(str(e)) + return False + + return True + + def computeStressRatioReal( + self: Self, inputAttribute: AttributeEnum, outputAttribute: AttributeEnum + ) -> bool: + """Compute the ratio between horizontal and vertical effective stress. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + stressRatioRealAttributeName = outputAttribute.attributeName + if not isAttributeInObject( + self.m_output, stressRatioRealAttributeName, self.m_attributeOnPoints + ): + try: + stressAttributeName: str = inputAttribute.attributeName + stress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, stressAttributeName, self.m_attributeOnPoints + ) + assert stress is not None, ( + f"{stressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + verticalStress: npt.NDArray[np.float64] = stress[:, 2] + # keep the minimum of the 2 horizontal components + horizontalStress: npt.NDArray[np.float64] = np.min( + stress[:, :2], axis=1 + ) + + stressRatioReal: npt.NDArray[np.float64] = fcts.stressRatio( + horizontalStress, verticalStress + ) + createAttribute( + self.m_output, + stressRatioReal, + stressRatioRealAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error( + f"{outputAttribute.attributeName} was not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + return True + + def computeEffectiveStressRatioOed(self: Self) -> bool: + """Compute the effective stress ratio in oedometric conditions. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + effectiveStressRatioOedAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_EFFECTIVE_RATIO_OED.attributeName + ) + if not isAttributeInObject( + self.m_output, + effectiveStressRatioOedAttributeName, + self.m_attributeOnPoints, + ): + poissonRatioAttributeName: str = ( + PostProcessingOutputsEnum.POISSON_RATIO.attributeName + ) + poissonRatio: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, poissonRatioAttributeName, self.m_attributeOnPoints + ) + + try: + assert poissonRatio is not None, ( + f"{poissonRatioAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + + effectiveStressRatioOed: npt.NDArray[np.float64] = ( + fcts.deviatoricStressPathOed(poissonRatio) + ) + createAttribute( + self.m_output, + effectiveStressRatioOed, + effectiveStressRatioOedAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error( + "Oedometric effective stress ratio was not computed due to:" + ) + self.m_logger.error(str(e)) + return False + return True + + def computeCriticalTotalStressRatio(self: Self) -> bool: + """Compute fracture index and fracture threshold. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + ret: bool = True + + fractureIndexAttributeName = ( + PostProcessingOutputsEnum.CRITICAL_TOTAL_STRESS_RATIO.attributeName + ) + if not isAttributeInObject( + self.m_output, fractureIndexAttributeName, self.m_attributeOnPoints + ): + + stressAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL.attributeName + ) + stress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, stressAttributeName, self.m_attributeOnPoints + ) + + pressureAttributeName: str = GeosMeshOutputsEnum.PRESSURE.attributeName + pressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, pressureAttributeName, self.m_attributeOnPoints + ) + + try: + assert stress is not None, ( + f"{stressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert pressure is not None, ( + f"{pressureAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert stress.shape[1] >= 3 + except AssertionError as e: + self.m_logger.error( + "Critical total stress ratio and threshold were not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + # fracture index + try: + verticalStress: npt.NDArray[np.float64] = stress[:, 2] + criticalTotalStressRatio: npt.NDArray[np.float64] = ( + fcts.criticalTotalStressRatio(pressure, verticalStress) + ) + createAttribute( + self.m_output, + criticalTotalStressRatio, + fractureIndexAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error( + "Critical total stress ratio was not computed due to:" + ) + self.m_logger.error(str(e)) + ret = False + + # fracture threshold + try: + mask: npt.NDArray[np.bool_] = np.argmin(np.abs(stress[:, :2]), axis=1) + horizontalStress: npt.NDArray[np.float64] = stress[:, :2][ + np.arange(stress[:, :2].shape[0]), mask + ] + + stressRatioThreshold: npt.NDArray[np.float64] = ( + fcts.totalStressRatioThreshold(pressure, horizontalStress) + ) + fractureThresholdAttributeName = ( + PostProcessingOutputsEnum.TOTAL_STRESS_RATIO_THRESHOLD.attributeName + ) + createAttribute( + self.m_output, + stressRatioThreshold, + fractureThresholdAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error( + "Total stress ratio threshold was not computed due to:" + ) + self.m_logger.error(str(e)) + ret = False + + return ret + + def computeCriticalPorePressure(self: Self) -> bool: + """Compute the critical pore pressure and the pressure index. + + Returns: + bool: return True if calculation successfully ended, False otherwise. + """ + ret: bool = True + criticalPorePressureAttributeName = ( + PostProcessingOutputsEnum.CRITICAL_PORE_PRESSURE.attributeName + ) + if not isAttributeInObject( + self.m_output, criticalPorePressureAttributeName, self.m_attributeOnPoints + ): + + stressAttributeName: str = ( + PostProcessingOutputsEnum.STRESS_TOTAL.attributeName + ) + stress: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, stressAttributeName, self.m_attributeOnPoints + ) + + pressureAttributeName: str = GeosMeshOutputsEnum.PRESSURE.attributeName + pressure: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, pressureAttributeName, self.m_attributeOnPoints + ) + + try: + assert self.m_rockCohesion is not None, "Rock cohesion is undefined." + assert self.m_frictionAngle is not None, "Friction angle is undefined." + assert stress is not None, ( + f"{stressAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert pressure is not None, ( + f"{pressureAttributeName}" + UNDEFINED_ATTRIBUTE_MESSAGE + ) + assert stress.shape[1] >= 3 + except AssertionError as e: + self.m_logger.error( + "Critical pore pressure and threshold were not computed due to:" + ) + self.m_logger.error(str(e)) + return False + + try: + criticalPorePressure: npt.NDArray[np.float64] = ( + fcts.criticalPorePressure( + -1.0 * stress, self.m_rockCohesion, self.m_frictionAngle + ) + ) + createAttribute( + self.m_output, + criticalPorePressure, + criticalPorePressureAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Critical pore pressure was not computed due to:") + self.m_logger.error(str(e)) + return False + + try: + # add critical pore pressure index (i.e., ratio between pressure and criticalPorePressure) + assert criticalPorePressure is not None, ( + "Critical pore pressure attribute" + " was not created" + ) + criticalPorePressureIndex: npt.NDArray[np.float64] = ( + fcts.criticalPorePressureThreshold(pressure, criticalPorePressure) + ) + criticalPorePressureIndexAttributeName = ( + PostProcessingOutputsEnum.CRITICAL_PORE_PRESSURE_THRESHOLD.attributeName + ) + createAttribute( + self.m_output, + criticalPorePressureIndex, + criticalPorePressureIndexAttributeName, + (), + self.m_attributeOnPoints, + ) + except AssertionError as e: + self.m_logger.error("Pore pressure threshold was not computed due to:") + self.m_logger.error(str(e)) + ret = False + + return ret + + def getPointCoordinates(self: Self) -> npt.NDArray[np.float64]: + """Get the coordinates of Points or Cell center. + + Returns: + npt.NDArray[np.float64]: points/cell center coordinates + """ + if self.m_attributeOnPoints: + return self.m_output.GetPoints() # type: ignore[no-any-return] + else: + # Find cell centers + filter = vtkCellCenters() + filter.SetInputDataObject(self.m_output) + filter.Update() + return filter.GetOutput().GetPoints() # type: ignore[no-any-return] diff --git a/geos-posp/src/geos_posp/filters/GeosBlockExtractor.py b/geos-posp/src/geos_posp/filters/GeosBlockExtractor.py new file mode 100644 index 00000000..1718bc3a --- /dev/null +++ b/geos-posp/src/geos_posp/filters/GeosBlockExtractor.py @@ -0,0 +1,312 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +from typing_extensions import Self +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkMultiBlockDataSet + +from geos_posp.processing.multiblockInpectorTreeFunctions import ( + getBlockIndexFromName, +) +from geos_posp.processing.vtkUtils import extractBlock +from geos_posp.utils.GeosOutputsConstants import ( + GeosDomainNameEnum, + OutputObjectEnum, +) +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +GeosBlockExtractor module is a vtk filter that allows to extract Volume mesh, +Wells and Faults from a vtkMultiBlockDataSet. + +Filter input and output types are vtkMultiBlockDataSet. + +To use the filter: + +.. code-block:: python + + from filters.GeosBlockExtractor import GeosBlockExtractor + + # filter inputs + logger :Logger + input :vtkMultiBlockDataSet + + # instanciate the filter + blockExtractor :GeosBlockExtractor = GeosBlockExtractor() + # set the logger + blockExtractor.SetLogger(logger) + # set input data object + blockExtractor.SetInputDataObject(input) + # ExtractFaultsOn or ExtractFaultsOff to (de)activate the extraction of Fault blocks + blockExtractor.ExtractFaultsOn() + # ExtractWellsOn or ExtractWellsOff to (de)activate the extraction of well blocks + blockExtractor.ExtractWellsOn() + # do calculations + blockExtractor.Update() + # get output object + output :vtkMultiBlockDataSet = blockExtractor.GetOutputDataObject(0) +""" + + +class GeosBlockExtractor(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """VTK Filter that perform GEOS block extraction. + + The filter returns the volume mesh as the first output, Surface mesh as the second + output, and well mesh as the third output. + """ + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkMultiBlockDataSet") # type: ignore[no-untyped-call] + + self.m_extractFaults: bool = False + self.m_extractWells: bool = False + self.m_outputPortMapping: dict[OutputObjectEnum, int] = { + OutputObjectEnum.VOLUME: 0, + OutputObjectEnum.FAULTS: -1, + OutputObjectEnum.WELLS: -1, + } + + self.m_input: vtkMultiBlockDataSet + self.m_outputVolumeMesh: vtkMultiBlockDataSet + self.m_outputFaults: vtkMultiBlockDataSet + self.m_outputWells: vtkMultiBlockDataSet + + self.m_logger: Logger = getLogger("Geos Block Extractor Filter") + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + self.m_input = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + assert self.m_input is not None, "Input object is null." + + # initialize output objects + volumeMeshPort: int = self.m_outputPortMapping[OutputObjectEnum.VOLUME] + self.m_outputVolumeMesh = self.GetOutputData(outInfoVec, volumeMeshPort) # type: ignore[no-untyped-call] + assert self.m_outputVolumeMesh is not None, "Output volume mesh is null." + + if self.m_extractFaults: + faultMeshPort: int = self.m_outputPortMapping[OutputObjectEnum.FAULTS] + assert faultMeshPort > 0, "Faults output port is undefined." + assert ( + faultMeshPort < self.GetNumberOfOutputPorts() + ), "Number of output ports is unconsistent with output objects." + self.m_outputFaults = self.GetOutputData(outInfoVec, faultMeshPort) # type: ignore[no-untyped-call] + assert self.m_outputFaults is not None, "Output surface mesh is null." + + if self.m_extractWells: + wellMeshPort: int = self.m_outputPortMapping[OutputObjectEnum.WELLS] + assert wellMeshPort > 0, "Wells output port is undefined." + assert ( + wellMeshPort < self.GetNumberOfOutputPorts() + ), "Number of output ports is unconsistent with output objects." + self.m_outputWells = self.GetOutputData(outInfoVec, wellMeshPort) # type: ignore[no-untyped-call] + assert self.m_outputWells is not None, "Output well mesh is null." + + self.doExtraction() + + except AssertionError as e: + mess: str = "Geos block extraction failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Geos block extraction failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def SetLogger(self: Self, logger: Logger) -> None: + """Set the logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def UpdateOutputPorts(self: Self) -> None: + """Set the number of output ports and update extraction options.""" + # update number of output port + nOutputPort: int = 1 + if self.m_extractFaults: + nOutputPort += 1 + if self.m_extractWells: + nOutputPort += 1 + self.SetNumberOfOutputPorts(nOutputPort) + + # update output port mapping + self.m_outputPortMapping[OutputObjectEnum.FAULTS] = -1 + self.m_outputPortMapping[OutputObjectEnum.WELLS] = -1 + if nOutputPort == 2: + outputObject: OutputObjectEnum = ( + OutputObjectEnum.FAULTS + if self.m_extractFaults + else OutputObjectEnum.WELLS + ) + self.m_outputPortMapping[outputObject] = 1 + else: + self.m_outputPortMapping[OutputObjectEnum.FAULTS] = 1 + self.m_outputPortMapping[OutputObjectEnum.WELLS] = 2 + + def ExtractFaultsOn(self: Self) -> None: + """Activate the extraction of Faults.""" + self.m_extractFaults = True + self.UpdateOutputPorts() + + def ExtractFaultsOff(self: Self) -> None: + """Deactivate the extraction of Faults.""" + self.m_extractFaults = False + self.UpdateOutputPorts() + + def ExtractWellsOn(self: Self) -> None: + """Activate the extraction of Wells.""" + self.m_extractWells = True + self.UpdateOutputPorts() + + def ExtractWellsOff(self: Self) -> None: + """Deactivate the extraction of Wells.""" + self.m_extractWells = False + self.UpdateOutputPorts() + + def getOutputVolume(self: Self) -> vtkMultiBlockDataSet: + """Get output volume mesh. + + Returns: + vtkMultiBlockDataSet: volume mesh + """ + return self.m_outputVolumeMesh + + def getOutputFaults(self: Self) -> vtkMultiBlockDataSet: + """Get output fault mesh. + + Returns: + vtkMultiBlockDataSet: fault mesh + """ + assert ( + self.m_extractFaults + ), "Extract fault option was set to False, turn on first." + return self.m_outputFaults + + def getOutputWells(self: Self) -> vtkMultiBlockDataSet: + """Get output well mesh. + + Returns: + vtkMultiBlockDataSet: well mesh + """ + assert ( + self.m_extractWells + ), "Extract well option was set to False, turn on first." + return self.m_outputWells + + def doExtraction(self: Self) -> int: + """Apply block extraction. + + Returns: + bool: True if block extraction successfully ended, False otherwise. + """ + try: + assert self.m_input is not None, "Input mesh is null." + + if not self.extractRegion(GeosDomainNameEnum.VOLUME_DOMAIN_NAME): + self.m_logger.error("Volume mesh extraction failed.") + if self.m_extractFaults and not self.extractRegion( + GeosDomainNameEnum.FAULT_DOMAIN_NAME + ): + self.m_logger.error("Fault extraction failed.") + if self.m_extractWells and not self.extractRegion( + GeosDomainNameEnum.WELL_DOMAIN_NAME + ): + self.m_logger.error("Well extraction failed.") + except AssertionError as e: + mess: str = "Block extraction failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess1: str = "Block extraction failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def extractRegion(self: Self, type: GeosDomainNameEnum) -> int: + """Extract volume mesh from input vtkMultiBlockDataSet. + + Returns: + bool: True if volume mesh extraction successfully ended, False otherwise. + """ + block: vtkMultiBlockDataSet + blockIndex = getBlockIndexFromName(self.m_input, type.value) + if blockIndex < 0: + self.m_logger.warning("Cell block index is invalid.") + return 0 + + block = extractBlock(self.m_input, blockIndex) + assert block is not None, f"Extracted {type.value} block is null." + + if (type is GeosDomainNameEnum.VOLUME_DOMAIN_NAME) and ( + self.m_outputVolumeMesh is not None + ): + self.m_outputVolumeMesh.ShallowCopy(block) + self.m_outputVolumeMesh.Modified() + elif (type is GeosDomainNameEnum.FAULT_DOMAIN_NAME) and ( + self.m_outputFaults is not None + ): + self.m_outputFaults.ShallowCopy(block) + self.m_outputFaults.Modified() + elif (type is GeosDomainNameEnum.WELL_DOMAIN_NAME) and ( + self.m_outputWells is not None + ): + self.m_outputWells.ShallowCopy(block) + self.m_outputWells.Modified() + else: + raise TypeError(f"Output object for domain {type.value} is null.") + return 1 diff --git a/geos-posp/src/geos_posp/filters/GeosBlockMerge.py b/geos-posp/src/geos_posp/filters/GeosBlockMerge.py new file mode 100644 index 00000000..4cf51346 --- /dev/null +++ b/geos-posp/src/geos_posp/filters/GeosBlockMerge.py @@ -0,0 +1,535 @@ +# SPDX-License-Identifier: Apache-2.0 +# # SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file + +from typing_extensions import Self +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCompositeDataSet, + vtkDataObjectTreeIterator, + vtkMultiBlockDataSet, + vtkPolyData, + vtkUnstructuredGrid, +) +from vtkmodules.vtkFiltersCore import ( + vtkArrayRename, + vtkPolyDataNormals, + vtkPolyDataTangents, +) +from vtkmodules.vtkFiltersGeometry import vtkDataSetSurfaceFilter +from vtkmodules.vtkFiltersTexture import vtkTextureMapToPlane + +from geos_posp.processing.multiblockInpectorTreeFunctions import ( + getElementaryCompositeBlockIndexes, +) +from geos_posp.processing.vtkUtils import ( + createConstantAttribute, + extractBlock, + fillAllPartialAttributes, + getAttributeSet, + mergeBlocks, +) +from geos_posp.utils.GeosOutputsConstants import ( + PHASE_SEP, + FluidPrefixEnum, + PhaseTypeEnum, + PostProcessingOutputsEnum, + getRockSuffixRenaming, +) +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +GeosBlockMerge module is a vtk filter that allows to merge Geos ranks, rename +stress and porosity attributes, and identify fluids and rock phases. + +Filter input and output types are vtkMultiBlockDataSet. + +To use the filter: + +.. code-block:: python + + from filters.GeosBlockMerge import GeosBlockMerge + + # filter inputs + logger :Logger + input :vtkMultiBlockDataSet + + # instanciate the filter + mergeBlockFilter :GeosBlockMerge = GeosBlockMerge() + # set the logger + mergeBlockFilter.SetLogger(logger) + # set input data object + mergeBlockFilter.SetInputDataObject(input) + # ConvertSurfaceMeshOff or ConvertSurfaceMeshOn to (de)activate the conversion + # of vtkUnstructuredGrid to surface withNormals and Tangents calculation. + mergeBlockFilter.ConvertSurfaceMeshOff() + # do calculations + mergeBlockFilter.Update() + # get output object + output :vtkMultiBlockDataSet = mergeBlockFilter.GetOutputDataObject(0) +""" + + +class GeosBlockMerge(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """VTK Filter that perform GEOS rank merge. + + The filter returns a multiblock mesh composed of elementary blocks. + + """ + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkMultiBlockDataSet") # type: ignore[no-untyped-call] + + self.m_input: vtkMultiBlockDataSet + self.m_output: vtkMultiBlockDataSet + + self.m_convertFaultToSurface: bool = True + + # set logger + self.m_logger: Logger = getLogger("Geos Block Merge Filter") + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkMultiBlockDataSet") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + self.m_input = vtkMultiBlockDataSet.GetData(inInfoVec[0]) + + # initialize output objects + self.m_output = self.GetOutputData(outInfoVec, 0) # type: ignore[no-untyped-call] + + assert self.m_input is not None, "Input object is null." + assert self.m_output is not None, "Output object is null." + + self.doMerge() + + except AssertionError as e: + mess: str = "Geos block merge failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Geos block merge failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def SetLogger(self: Self, logger: Logger) -> None: + """Set the logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def ConvertSurfaceMeshOn(self: Self) -> None: + """Activate surface conversion from vtkUnstructredGrid to vtkPolyData.""" + self.m_convertFaultToSurface = True + + def ConvertSurfaceMeshOff(self: Self) -> None: + """Deactivate surface conversion from vtkUnstructredGrid to vtkPolyData.""" + self.m_convertFaultToSurface = False + + def doMerge(self: Self) -> int: + """Apply block merge. + + Returns: + bool: True if block merge successfully ended, False otherwise. + """ + try: + self.mergeRankBlocks() + if self.m_convertFaultToSurface: + self.convertFaultsToSurfaces() + assert self.m_outputMesh is not None, "Output mesh in null." + self.m_output.ShallowCopy(self.m_outputMesh) + except AssertionError as e: + mess: str = "Block merge failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess1: str = "Block merge failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def mergeRankBlocks(self: Self) -> bool: + """Merge all elementary node that belong to a same parent node. + + Returns: + bool: True if calculation successfully ended, False otherwise + """ + # display phase names + try: + phaseClassification: dict[str, PhaseTypeEnum] = self.getPhases(True) + if phaseClassification is not None: + for phaseTypeRef in list(PhaseTypeEnum): + phases = [ + phaseName + for phaseName, phaseType in phaseClassification.items() + if phaseType is phaseTypeRef + ] + if len(phases) > 0: + self.m_logger.info( + f"Identified {phaseTypeRef.type} phase(s) are: {phases}" + ) + except AssertionError as e: + self.m_logger.warning("Phases were not identified due to:") + self.m_logger.warning(e) + + compositeBlockIndexesToMerge: dict[str, int] = ( + getElementaryCompositeBlockIndexes(self.m_input) + ) + nbBlocks: int = len(compositeBlockIndexesToMerge) + self.m_outputMesh = vtkMultiBlockDataSet() + self.m_outputMesh.SetNumberOfBlocks(nbBlocks) + for newIndex, (blockName, blockIndex) in enumerate( + compositeBlockIndexesToMerge.items() + ): + # extract composite block + blockToMerge1: vtkMultiBlockDataSet = extractBlock(self.m_input, blockIndex) + assert blockToMerge1 is not None, "Extracted block to merge is null." + + # rename attributes + blockToMerge2: vtkMultiBlockDataSet = self.renameAttributes( + blockToMerge1, phaseClassification + ) + assert blockToMerge2 is not None, "Attribute renaming failed." + + # merge all its children + mergedBlock: vtkUnstructuredGrid = self.mergeChildBlocks(blockToMerge2) + assert mergedBlock is not None, "Merged block is null." + + # create index attribute keeping the index in intial mesh + if not createConstantAttribute( + mergedBlock, + [ + blockIndex, + ], + PostProcessingOutputsEnum.BLOCK_INDEX.attributeName, + (), + False, + ): + self.m_logger.warning("BlockIndex attribute was not created.") + + # set this composite block into the output + self.m_outputMesh.SetBlock(newIndex, mergedBlock) + self.m_outputMesh.GetMetaData(newIndex).Set( + vtkCompositeDataSet.NAME(), blockName + ) + + assert ( + self.m_outputMesh.GetNumberOfBlocks() == nbBlocks + ), "Final number of merged blocks is wrong." + return True + + def renameAttributes( + self: Self, + mesh: vtkMultiBlockDataSet, + phaseClassification: dict[str, PhaseTypeEnum], + ) -> vtkMultiBlockDataSet: + """Rename attributes to harmonize throughout the mesh. + + Args: + mesh (vtkMultiBlockDataSet): input mesh + phaseClassification (dict[str, PhaseTypeEnum]): phase classification + detected from attributes + + Returns: + vtkMultiBlockDataSet: output mesh with renamed attributes + """ + assert phaseClassification is not None, "Phases were not correctly identified." + + renameFilter: vtkArrayRename = vtkArrayRename() + renameFilter.SetInputData(mesh) + rockPhase: list[str] = [ + phaseName + for phaseName, phaseType in phaseClassification.items() + if phaseType is PhaseTypeEnum.ROCK + ] + for attributeName in getAttributeSet(mesh, False): + for phaseName in rockPhase: + if phaseName in attributeName: + for suffix, newName in getRockSuffixRenaming().items(): + if suffix in attributeName: + renameFilter.SetCellArrayName(attributeName, newName) + + renameFilter.Update() + output: vtkMultiBlockDataSet = renameFilter.GetOutput() + return output + + def getPhaseNames(self: Self, attributeSet: set[str]) -> set[str]: + """Get the names of the phases in the mesh from Point/Cell attributes. + + Args: + attributeSet (set[str]): list of attributes where to find phases + + Returns: + set[str]: the list of phase names that appear at least twice. + """ + phaseNameDict: dict[str, int] = {} + for name in attributeSet: + if PHASE_SEP in name: + # use the last occurence of PHASE_SEP to split phase name from + # property name + index = name.rindex(PHASE_SEP) + phaseName: str = name[:index] + if phaseName in phaseNameDict: + phaseNameDict[phaseName] += 1 + else: + phaseNameDict[phaseName] = 1 + + # remove names that appear only once + return set(phaseNameDict.keys()) + + def getPhases(self: Self, onCells: bool = True) -> dict[str, PhaseTypeEnum]: + """Get the dictionnary of phases classified according to PhaseTypeEnum. + + Args: + onCells (bool, optional): Attributes are on Cells (Default) or on + Points. + + Defaults to True. + + Returns: + dict[str, PhaseTypeEnum]: a dictionnary with phase names as keys and + phase type as value. + """ + attributeSet: set[str] = getAttributeSet(self.m_input, not onCells) + assert len(attributeSet) > 0, "Input object does not have any attribute." + + phaseClassification: dict[str, PhaseTypeEnum] = {} + phaseNames: set[str] = self.getPhaseNames(attributeSet) + for phaseName in phaseNames: + # check for fluid phase names (most often the same names: fluid, water, or gas) + if any( + fluidPrefix.value.lower() in phaseName.lower() + for fluidPrefix in list(FluidPrefixEnum) + ): + phaseClassification[phaseName] = PhaseTypeEnum.FLUID + continue + + for attributeName in attributeSet: + if phaseName in attributeName: + index = attributeName.index(phaseName) + len(phaseName) + suffix = attributeName[index:] + for phaseType in list(PhaseTypeEnum): + if suffix in phaseType.attributes: + if (phaseName in phaseClassification) and ( + phaseType is not phaseClassification[phaseName] + ): + self.m_logger.warning( + f"The phase {phaseName} may be misclassified " + + "since the same name is used for both " + + "{phaseType.type} and " + + "{phaseClassification[phaseName].type} types" + ) + phaseClassification[phaseName] = phaseType + + return phaseClassification + + def mergeChildBlocks( + self: Self, compositeBlock: vtkMultiBlockDataSet + ) -> vtkUnstructuredGrid: + """Merge all children of the input composite block. + + Args: + compositeBlock (vtkMultiBlockDataSet): composite block + + Returns: + vtkUnstructuredGrid: merged block + """ + # fill partial cell attributes in all children blocks + if not fillAllPartialAttributes(compositeBlock, False): + self.m_logger.warning( + "Some partial cell attributes may not have been " + + "propagated to the whole mesh." + ) + + # # fill partial point attributes in all children blocks + if not fillAllPartialAttributes(compositeBlock, True): + self.m_logger.warning( + "Some partial point attributes may not have been " + + "propagated to the whole mesh." + ) + + # merge blocks + return mergeBlocks(compositeBlock) + + def convertFaultsToSurfaces(self: Self) -> bool: + """Convert blocks corresponding to faults to surface. + + Returns: + bool: True if calculation succesfully ended, False otherwise + """ + assert self.m_outputMesh is not None, "Output surface is null." + + transientMesh: vtkMultiBlockDataSet = vtkMultiBlockDataSet() + nbSurfaces: int = self.m_outputMesh.GetNumberOfBlocks() + transientMesh.SetNumberOfBlocks(nbSurfaces) + + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(self.m_outputMesh) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + surfaceIndex: int = 0 + while iter.GetCurrentDataObject() is not None: + surfaceName: str = iter.GetCurrentMetaData().Get(vtkCompositeDataSet.NAME()) + # convert block to surface + surface0: vtkUnstructuredGrid = vtkUnstructuredGrid.SafeDownCast( + iter.GetCurrentDataObject() + ) + surface1: vtkPolyData = self.convertBlockToSurface(surface0) + assert surface1 is not None, "Surface extraction from block failed." + # compute normals + surface2: vtkPolyData = self.computeNormals(surface1) + assert surface2 is not None, "Normal calculation failed." + # compute tangents + surface3: vtkPolyData = self.computeTangents(surface2) + assert surface3 is not None, "Tangent calculation failed." + + # set surface to output multiBlockDataSet + transientMesh.SetBlock(surfaceIndex, surface3) + transientMesh.GetMetaData(surfaceIndex).Set( + vtkCompositeDataSet.NAME(), surfaceName + ) + + iter.GoToNextItem() + surfaceIndex += 1 + + self.m_outputMesh.ShallowCopy(transientMesh) + return True + + def convertBlockToSurface(self: Self, block: vtkUnstructuredGrid) -> vtkPolyData: + """Convert vtkUnstructuredGrid to a surface vtkPolyData. + + ..WARNING: work only with triangulated surfaces + + TODO: need to convert quadrangular to triangulated surfaces first + + + Args: + block (vtkUnstructuredGrid): block from which to extract the surface + + Returns: + vtkPolyData: extracted surface + """ + extractSurfaceFilter: vtkDataSetSurfaceFilter = vtkDataSetSurfaceFilter() + extractSurfaceFilter.SetInputData(block) + # fast mode should be used for rendering only + extractSurfaceFilter.FastModeOff() + # Delegation activated allow to accelerate the processing with unstructured mesh + # see https://vtk.org/doc/nightly/html/classvtkDataSetSurfaceFilter.html + extractSurfaceFilter.DelegationOn() + extractSurfaceFilter.Update() + output: vtkPolyData = extractSurfaceFilter.GetOutput() + return output + + def computeNormals(self: Self, surface: vtkPolyData) -> vtkPolyData: + """Compute normals of the given surface. + + Args: + surface (vtkPolyData): surface to compute the normals + + Returns: + vtkPolyData: surface with normal attribute + """ + normalFilter: vtkPolyDataNormals = vtkPolyDataNormals() + normalFilter.SetInputData(surface) + normalFilter.ComputeCellNormalsOn() + normalFilter.ComputePointNormalsOff() + normalFilter.Update() + output: vtkPolyData = normalFilter.GetOutput() + return output + + def computeTangents(self: Self, surface: vtkPolyData) -> vtkPolyData: + """Compute tangents of the given surface. + + Args: + surface (vtkPolyData): surface to compute the tangents + + Returns: + vtkPolyData: surface with tangent attribute + """ + # need to compute texture coordinates required for tangent calculation + textureFilter: vtkTextureMapToPlane = vtkTextureMapToPlane() + textureFilter.SetInputData(surface) + textureFilter.AutomaticPlaneGenerationOn() + textureFilter.Update() + surface1: vtkPolyData = textureFilter.GetOutput() + assert ( + surface1 is not None + ), "Texture calculation during Tangent calculation failed." + + # compute tangents + tangentFilter: vtkPolyDataTangents = vtkPolyDataTangents() + tangentFilter.SetInputData(surface1) + tangentFilter.ComputeCellTangentsOn() + tangentFilter.ComputePointTangentsOff() + tangentFilter.Update() + surfaceOut: vtkPolyData = tangentFilter.GetOutput() + assert surfaceOut is not None, "Tangent components calculation failed." + + # copy tangents attributes into filter input surface because surface attributes + # are not transferred to the output (bug that should be corrected by Kitware) + array: vtkDataArray = surfaceOut.GetCellData().GetTangents() + assert array is not None, "Attribute Tangents is not in the mesh." + + surface1.GetCellData().SetTangents(array) + surface1.GetCellData().Modified() + surface1.Modified() + return surface1 diff --git a/geos-posp/src/geos_posp/filters/SurfaceGeomechanics.py b/geos-posp/src/geos_posp/filters/SurfaceGeomechanics.py new file mode 100644 index 00000000..d1e2d8a9 --- /dev/null +++ b/geos-posp/src/geos_posp/filters/SurfaceGeomechanics.py @@ -0,0 +1,491 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import numpy as np +import numpy.typing as npt +import vtkmodules.util.numpy_support as vnp +from typing_extensions import Self +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkDoubleArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import ( + vtkPolyData, +) + +import geos_posp.processing.geomechanicsCalculatorFunctions as fcts +import geos_posp.processing.geometryFunctions as geom +from geos_posp.processing.vtkUtils import ( + createAttribute, + getArrayInObject, + getAttributeSet, + isAttributeInObject, +) +from geos_posp.utils.GeosOutputsConstants import ( + ComponentNameEnum, + GeosMeshOutputsEnum, + PostProcessingOutputsEnum, + getAttributeToConvertFromLocalToXYZ, +) +from geos_posp.utils.geosUtils import ( + getAttributeMatrixFromVector, + getAttributeVectorFromMatrix, +) +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + DEFAULT_FRICTION_ANGLE_RAD, + DEFAULT_ROCK_COHESION, +) + +__doc__ = """ +SurfaceGeomechanics module is a vtk filter that allows to compute Geomechanical +properties on surfaces. + +Filter input and output types are vtkPolyData. + +To use the filter: + +.. code-block:: python + + from filters.SurfaceGeomechanics import SurfaceGeomechanics + + # filter inputs + logger :Logger + input :vtkPolyData + rockCohesion :float + frictionAngle :float # angle in radian + + # instanciate the filter + surfaceGeomechanicsFilter :SurfaceGeomechanics = SurfaceGeomechanics() + # set the logger + surfaceGeomechanicsFilter.SetLogger(logger) + # set input data object + surfaceGeomechanicsFilter.SetInputDataObject(input) + # set rock cohesion anf friction angle + surfaceGeomechanicsFilter.SetRockCohesion(rockCohesion) + surfaceGeomechanicsFilter.SetFrictionAngle(frictionAngle) + # do calculations + surfaceGeomechanicsFilter.Update() + # get output object + output :vtkPolyData = surfaceGeomechanicsFilter.GetOutputDataObject(0) + # get created attribute names + newAttributeNames :set[str] = surfaceGeomechanicsFilter.GetNewAttributeNames() +""" + + +class SurfaceGeomechanics(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Vtk filter to compute geomechanical surfacic attributes. + + Input and Output objects are a vtkMultiBlockDataSet containing surface + objects with Normals and Tangential attributes. + """ + super().__init__(nInputPorts=1, nOutputPorts=1, outputType="vtkPolyData") # type: ignore[no-untyped-call] + + # output surface mesh + self.m_output: vtkPolyData + # attributes are either on points or on cells + self.m_attributeOnPoints: bool = False + # rock cohesion (Pa) + self.m_rockCohesion: float = DEFAULT_ROCK_COHESION + # friction angle (rad) + self.m_frictionAngle: float = DEFAULT_FRICTION_ANGLE_RAD + # new created attributes names + self.m_newAttributeNames: set[str] = set() + + # logger + self.m_logger: Logger = getLogger("Surface Geomechanics Filter") + + def SetRockCohesion(self: Self, rockCohesion: float) -> None: + """Set rock cohesion value. + + Args: + rockCohesion (float): rock cohesion (Pa) + """ + self.m_rockCohesion = rockCohesion + + def SetFrictionAngle(self: Self, frictionAngle: float) -> None: + """Set friction angle value. + + Args: + frictionAngle (float): friction angle (rad) + """ + self.m_frictionAngle = frictionAngle + + def SetLogger(self: Self, logger: Logger) -> None: + """Set the logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def GetNewAttributeNames(self: Self) -> set[str]: + """Get the set of new attribute names that were created. + + Returns: + set[str]: set of new attribute names + """ + return self.m_newAttributeNames + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkPolyData") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + input = vtkPolyData.GetData(inInfoVec[0]) + self.m_output = self.GetOutputData(outInfoVec, 0) # type: ignore[no-untyped-call] + + assert input is not None, "Input object is null." + assert self.m_output is not None, "Output pipeline is null." + + self.m_output.ShallowCopy(input) + # conversion of vectorial attributes from Normal/Tangent basis to xyz basis + assert ( + self.convertLocalToXYZBasisAttributes() + ), "Error while converting Local to XYZ basis attributes" + # compute shear capacity utilization + assert self.computeShearCapacityUtilization(), "Error while computing SCU." + self.Modified() + except AssertionError as e: + mess: str = "Surface geomechanics attributes calculation failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess1: str = "Surface geomechanics attributes calculation failed due to:" + self.m_logger.critical(mess1) + self.m_logger.critical(e, exc_info=True) + return 0 + mess2: str = "Surface geomechanics attributes were successfully computed." + self.m_logger.info(mess2) + return 1 + + def convertLocalToXYZBasisAttributes(self: Self) -> bool: + """Convert vectorial property coordinates from Local to canonic basis. + + Returns: + bool: True if calculation successfully ended, False otherwise + """ + # look for the list of attributes to convert + attributesToConvert: set[str] = self.getAttributesToConvertFromLocalToXYZ() + if len(attributesToConvert) == 0: + self.m_logger.info( + "No attribute to convert from local to XYZ basis were found." + ) + return False + + # get local coordinate vectors + normalTangentVectors: npt.NDArray[np.float64] = self.getNormalTangentsVectors() + # do conversion for each attribute + for attributName in attributesToConvert: + # skip attribute if it is already in the object + newAttrName: str = attributName + "_" + ComponentNameEnum.XYZ.name + if isAttributeInObject(self.m_output, newAttrName, False): + continue + + attr: vtkDoubleArray = self.m_output.GetCellData().GetArray(attributName) + assert attr is not None, "Attribute {attributName} is undefined." + assert attr.GetNumberOfComponents() > 2, ( + "Dimension of the attribute " + " must be equal or grater than 3." + ) + + attrArray: npt.NDArray[np.float64] = vnp.vtk_to_numpy(attr) # type: ignore[no-untyped-call] + newAttrArray: npt.NDArray[np.float64] = self.computeNewCoordinates( + attrArray, normalTangentVectors, True + ) + + # create attribute + createAttribute( + self.m_output, + newAttrArray, + newAttrName, + ComponentNameEnum.XYZ.value, + False, + ) + self.m_newAttributeNames.add(newAttrName) + return True + + def convertXYZToLocalBasisAttributes(self: Self) -> bool: + """Convert vectorial property coordinates from canonic to local basis. + + Returns: + bool: True if calculation successfully ended, False otherwise + """ + # look for the list of attributes to convert + # empty but to update if needed in the future + attributesToConvert: set[str] = set() + if len(attributesToConvert) == 0: + self.m_logger.info( + "No attribute to convert from local to " + "canonic basis were found." + ) + return False + + # get local coordinate vectors + normalTangentVectors: npt.NDArray[np.float64] = self.getNormalTangentsVectors() + for attributName in attributesToConvert: + # skip attribute if it is already in the object + newAttrName: str = ( + attributName + "_" + ComponentNameEnum.NORMAL_TANGENTS.name + ) + if isAttributeInObject(self.m_output, newAttrName, False): + continue + attr: vtkDoubleArray = self.m_output.GetCellData().GetArray(attributName) + assert attr is not None, "Attribute {attributName} is undefined." + assert attr.GetNumberOfComponents() > 2, ( + "Dimension of the attribute " + " must be equal or grater than 3." + ) + + attrArray: npt.NDArray[np.float64] = vnp.vtk_to_numpy(attr) # type: ignore[no-untyped-call] + newAttrArray: npt.NDArray[np.float64] = self.computeNewCoordinates( + attrArray, normalTangentVectors, False + ) + + # create attribute + createAttribute( + self.m_output, + newAttrArray, + newAttrName, + ComponentNameEnum.NORMAL_TANGENTS.value, + False, + ) + self.m_newAttributeNames.add(newAttrName) + return True + + def getAttributesToConvertFromLocalToXYZ(self: Self) -> set[str]: + """Get the list of attributes to convert from local to XYZ basis. + + Returns: + set[str]: Set of the attribute names. + """ + return self.filterAttributesToConvert(getAttributeToConvertFromLocalToXYZ()) + + def filterAttributesToConvert( + self: Self, attributesToFilter0: set[str] + ) -> set[str]: + """Filter the set of attribute names if they are vectorial and present. + + Args: + attributesToFilter0 (set[str]): set of attribute names to filter. + + Returns: + set[str]: Set of the attribute names. + """ + attributesFiltered: set[str] = set() + attributeSet: set[str] = getAttributeSet(self.m_output, False) + for attributName in attributesToFilter0: + if attributName in attributeSet: + attr: vtkDataArray = self.m_output.GetCellData().GetArray(attributName) + if attr.GetNumberOfComponents() > 2: + attributesFiltered.add(attributName) + return attributesFiltered + + def computeNewCoordinates( + self: Self, + attrArray: npt.NDArray[np.float64], + normalTangentVectors: npt.NDArray[np.float64], + fromLocalToYXZ: bool, + ) -> npt.NDArray[np.float64]: + """Compute the coordinates of a vectorial attribute. + + Args: + attrArray (npt.NDArray[np.float64]): vector of attribute values + normalTangentVectors (npt.NDArray[np.float64]): 3xNx3 local vector + coordinates + fromLocalToYXZ (bool): if True, conversion is done from local to XYZ + basis, otherwise conversion is done from XZY to Local basis. + + Returns: + npt.NDArray[np.float64]: Vector of new coordinates of the attribute. + """ + attrArrayNew = np.full_like(attrArray, np.nan) + # for each cell + for i in range(attrArray.shape[0]): + # get the change of basis matrix + localBasis: npt.NDArray[np.float64] = normalTangentVectors[:, i, :] + changeOfBasisMatrix = self.computeChangeOfBasisMatrix( + localBasis, fromLocalToYXZ + ) + if attrArray.shape[1] == 3: + attrArrayNew[i] = self.computeNewCoordinatesVector3( + attrArray[i], changeOfBasisMatrix + ) + else: + attrArrayNew[i] = self.computeNewCoordinatesVector6( + attrArray[i], changeOfBasisMatrix + ) + + assert np.any( + np.isfinite(attrArrayNew) + ), "Attribute new coordinate calculation failed." + return attrArrayNew + + def computeNewCoordinatesVector3( + self: Self, + vector: npt.NDArray[np.float64], + changeOfBasisMatrix: npt.NDArray[np.float64], + ) -> npt.NDArray[np.float64]: + """Compute attribute new coordinates of vector of size 3. + + Args: + vector (npt.NDArray[np.float64]): input coordinates. + changeOfBasisMatrix (npt.NDArray[np.float64]): change of basis matrix + + Returns: + npt.NDArray[np.float64]: new coordinates + """ + return geom.computeCoordinatesInNewBasis(vector, changeOfBasisMatrix) + + def computeNewCoordinatesVector6( + self: Self, + vector: npt.NDArray[np.float64], + changeOfBasisMatrix: npt.NDArray[np.float64], + ) -> npt.NDArray[np.float64]: + """Compute attribute new coordinates of vector of size > 3. + + Args: + vector (npt.NDArray[np.float64]): input coordinates. + changeOfBasisMatrix (npt.NDArray[np.float64]): change of basis matrix + + Returns: + npt.NDArray[np.float64]: new coordinates + """ + attributeMatrix: npt.NDArray[np.float64] = getAttributeMatrixFromVector(vector) + attributeMatrixNew: npt.NDArray[np.float64] = np.full_like( + attributeMatrix, np.nan + ) + # for each column of the matrix + for j in range(attributeMatrix.shape[1]): + attributeMatrixNew[:, j] = geom.computeCoordinatesInNewBasis( + attributeMatrix[:, j], changeOfBasisMatrix + ) + return getAttributeVectorFromMatrix(attributeMatrixNew, vector.size) + + def computeChangeOfBasisMatrix( + self: Self, localBasis: npt.NDArray[np.float64], fromLocalToYXZ: bool + ) -> npt.NDArray[np.float64]: + """Compute the change of basis matrix according to local coordinates. + + Args: + localBasis (npt.NDArray[np.float64]): local coordinate vectors. + fromLocalToYXZ (bool): if True, change of basis matrix is from local + to XYZ bases, otherwise it is from XYZ to local bases. + + Returns: + npt.NDArray[np.float64]: change of basis matrix. + """ + P: npt.NDArray[np.float64] = np.transpose(localBasis) + if fromLocalToYXZ: + return P + # inverse the change of basis matrix + return np.linalg.inv(P) + + def getNormalTangentsVectors(self: Self) -> npt.NDArray[np.float64]: + """Compute the change of basis matrix from Local to XYZ bases. + + Returns: + npt.NDArray[np.float64]: Nx3 matrix of local vector coordinates. + """ + # get normal and first tangent components + normals: npt.NDArray[np.float64] = vnp.vtk_to_numpy( + self.m_output.GetCellData().GetNormals() + ) # type: ignore[no-untyped-call] + assert normals is not None, "Normal attribute was not found." + tangents1: npt.NDArray[np.float64] = vnp.vtk_to_numpy( + self.m_output.GetCellData().GetTangents() + ) # type: ignore[no-untyped-call] + assert tangents1 is not None, "Tangents attribute was not found." + + # compute second tangential component + tangents2: npt.NDArray[np.float64] = np.cross(normals, tangents1, axis=1) + assert tangents2 is not None, "Local basis third axis was not computed." + + # put vectors as columns + return np.array((normals, tangents1, tangents2)) + + def computeShearCapacityUtilization(self: Self) -> bool: + """Compute the shear capacity utilization on surface. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + try: + SCUAttributeName: str = PostProcessingOutputsEnum.SCU.attributeName + if not isAttributeInObject( + self.m_output, SCUAttributeName, self.m_attributeOnPoints + ): + tractionAttributeName: str = GeosMeshOutputsEnum.TRACTION.attributeName + traction: npt.NDArray[np.float64] = getArrayInObject( + self.m_output, tractionAttributeName, self.m_attributeOnPoints + ) + assert traction is not None, ( + f"{tractionAttributeName}" + " attribute is undefined." + ) + + scuAttribute: npt.NDArray[np.float64] = fcts.shearCapacityUtilization( + traction, self.m_rockCohesion, self.m_frictionAngle + ) + createAttribute( + self.m_output, + scuAttribute, + SCUAttributeName, + (), + self.m_attributeOnPoints, + ) + self.m_newAttributeNames.add(SCUAttributeName) + + except AssertionError as e: + self.m_logger.error("Shear Capacity Utilization was not computed due to:") + self.m_logger.error(str(e)) + return False + return True diff --git a/geos-posp/src/geos_posp/filters/TransferAttributesVolumeSurface.py b/geos-posp/src/geos_posp/filters/TransferAttributesVolumeSurface.py new file mode 100644 index 00000000..69324083 --- /dev/null +++ b/geos-posp/src/geos_posp/filters/TransferAttributesVolumeSurface.py @@ -0,0 +1,324 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import numpy as np +import numpy.typing as npt +import vtkmodules.util.numpy_support as vnp +from typing_extensions import Self +from vtk import VTK_DOUBLE # type: ignore[import-untyped] +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkInformation, + vtkInformationVector, +) +from vtkmodules.vtkCommonDataModel import vtkPolyData, vtkUnstructuredGrid + +from geos_posp.filters.VolumeSurfaceMeshMapper import VolumeSurfaceMeshMapper +from geos_posp.processing.ConnectionSet import ConnectionSetCollection +from geos_posp.processing.vtkUtils import ( + getArrayInObject, + getComponentNames, + isAttributeInObject, +) +from geos_posp.utils.GeosOutputsConstants import GeosMeshSuffixEnum +from geos_posp.utils.Logger import Logger, getLogger + +__doc__ = """ +TransferAttributesVolumeSurface is a vtk filter that allows to transfer volume +mesh attributes to surface mesh. + +This filter transfer a cell attribute as a face attribute from each volume cell +adjacent to a surface face. Since a face can be adjacent to 2 cells (one at +each side), 2 attributes are created with the suffix '_plus' and '_minus' +depending on the normal vector direction of the face. + +Input and output surface types are vtkPolyData and input volume mesh is +vtkUnstructuredGrid. + +.. WARNING:: + This filter must be use very cautiously since its result may have no sense. + + +To use it: + +.. code-block:: python + + from filters.TransferAttributesVolumeSurface import TransferAttributesVolumeSurface + + filter :TransferAttributesVolumeSurface = TransferAttributesVolumeSurface() + # set input data objects + filter.AddInputDataObject(0, volumeMesh) + filter.AddInputDataObject(1, surfaceMesh) + # set attribute names to transfer + attributeNames :set[str] + filter.SetAttributeNamesToTransfer(attributeNames) + # do calculations + filter.Update() + # get filter output surface with new attributes + output :vtkPolyData = filter.GetOutputDataObject(0) +""" + + +class TransferAttributesVolumeSurface(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Vtk filter to transfer attributes from volume to surface mesh. + + Input volume is vtkUnstructuredGrid and input, output surface mesh + is vtkPolyData, and the list of names of the attributes to transfer. + """ + super().__init__(nInputPorts=2, nOutputPorts=1, outputType="vtkPolyData") + + #: input volume mesh attributes are from + self.m_volumeMesh: vtkUnstructuredGrid + #: input surface mesh where to transfer attributes + self.m_surfaceMesh: vtkPolyData + #: output surface mesh + self.m_outputSurfaceMesh: vtkPolyData + #: set of attribute names to transfer + self.m_attributeNames: set[str] = set() + #: create attribute names + self.m_newAttributeNames: set[str] = set() + # logger + self.m_logger: Logger = getLogger( + "Attribute Transfer from Volume to Surface Filter" + ) + + def GetAttributeNamesToTransfer(self: Self) -> set[str]: + """Get the set of attribute names to transfer from volume to surface. + + Returns: + set[str]: set of attributes names. + """ + return self.m_attributeNames + + def SetAttributeNamesToTransfer(self: Self, names: set[str]) -> None: + """Set the set of attribute names to transfer from volume to surface. + + Args: + names (set[str]): set of attributes names. + """ + self.m_attributeNames = names + + def GetNewAttributeNames(self: Self) -> set[str]: + """Get the set of attribute names created in the output surface. + + Returns: + set[str]: Set of new attribute names in the surface. + """ + return self.m_newAttributeNames + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkUnstructuredGrid") + else: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkPolyData") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData1 = self.GetInputData(inInfoVec, 0, 0) + inData2 = self.GetInputData(inInfoVec, 1, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData1 is not None + assert inData2 is not None + if outData is None or (not outData.IsA(inData1.GetClassName())): + outData = inData1.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) # type: ignore[no-any-return] + + def RequestData( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + # input volume mesh + self.m_volumeMesh = vtkUnstructuredGrid.GetData(inInfoVec[0]) + # input surface + self.m_surfaceMesh = vtkPolyData.GetData(inInfoVec[1]) + # output volume mesh + self.m_outputSurfaceMesh = self.GetOutputData(outInfoVec, 0) + self.m_outputSurfaceMesh.ShallowCopy(self.m_surfaceMesh) + + # compute cell adjacency mapping + meshMap: ConnectionSetCollection = self.getMeshMapping() + # do transfer of attributes + self.doTransferAttributes(meshMap) + self.m_logger.info("Attribute transfer was successfully computed.") + except AssertionError as e: + mess: str = "Attribute transfer failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Attribute transfer failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def getMeshMapping(self: Self) -> ConnectionSetCollection: + """Compute cell mapping between volume and surface mesh. + + Returns: + dict[int, dict[int, bool]]: dictionnary of face ids as keys and + volume cell ids and side as values. + """ + + filter: VolumeSurfaceMeshMapper = VolumeSurfaceMeshMapper() + filter.AddInputDataObject(0, self.m_volumeMesh) + filter.AddInputDataObject(1, self.m_surfaceMesh) + filter.SetCreateAttribute(False) + filter.Update() + return filter.GetSurfaceToVolumeConnectionSets() + + def doTransferAttributes(self: Self, meshMap: ConnectionSetCollection) -> bool: + """Transfer all attributes from the set of attribute names. + + Except on boundaries, surfaces are bounded by cells along each side. + Two attributes are then created on the surface, one corresponding to + positive side cell values, one corresponding to negative side cell + values. + + Args: + meshMap (dict[int, dict[int, bool]]): map of surface face ids to + volume mesh cell ids and side. + + Returns: + bool: True if transfer successfully ended, False otherwise. + """ + for attributeName in self.m_attributeNames: + # negative side attribute + self.transferAttribute(attributeName, False, meshMap) + # positive side attribute + self.transferAttribute(attributeName, True, meshMap) + return True + + def transferAttribute( + self: Self, + attributeName: str, + surfaceSide: bool, + meshMap: ConnectionSetCollection, + ) -> bool: + """Transfer the attribute attributeName from volume to surface mesh. + + Created surface attribute will have the same name as input attribute + name with suffix "_Plus" for positive (True) side and "_Minus" for + negative (False) side. + + Args: + attributeName (str): Name of the attribute to transfer. + surfaceSide (bool): Side of the surface the attribute is from. + meshMap (dict[int, dict[int, bool]]): map of surface face ids to + volume mesh cell ids and side. + + Returns: + bool: True if transfer successfully ended, False otherwise. + """ + # get volume mesh attribute + if isAttributeInObject(self.m_volumeMesh, attributeName, False): + attr: npt.NDArray[np.float64] = getArrayInObject( + self.m_volumeMesh, attributeName, False + ) + attrComponentNames: tuple[str, ...] = getComponentNames( + self.m_volumeMesh, attributeName, False + ) + # creates attribute arrays on the surface + nbFaces: int = self.m_surfaceMesh.GetNumberOfCells() + nbComponents: int = ( + len(attrComponentNames) if len(attrComponentNames) > 0 else 1 + ) + suffix: str = ( + GeosMeshSuffixEnum.SURFACE_PLUS_SUFFIX.value + if surfaceSide + else GeosMeshSuffixEnum.SURFACE_MINUS_SUFFIX.value + ) + surfaceAttributeName: str = attributeName + suffix + attributeValues: npt.NDArray[np.float64] = np.full( + (nbFaces, nbComponents), np.nan + ) + + # for each face of the surface + for connectionSet in meshMap: + # for each cell of the volume mesh + for cellId, side in connectionSet.getConnectedCellIds().items(): + if side == surfaceSide: + attributeValues[connectionSet.getCellIdRef()] = attr[cellId] + + surfaceAttribute: vtkDataArray = vnp.numpy_to_vtk( + attributeValues, deep=True, array_type=VTK_DOUBLE + ) + surfaceAttribute.SetName(surfaceAttributeName) + if surfaceAttribute.GetNumberOfComponents() > 1: + for i in range(surfaceAttribute.GetNumberOfComponents()): + surfaceAttribute.SetComponentName(i, attrComponentNames[i]) + + self.m_outputSurfaceMesh.GetCellData().AddArray(surfaceAttribute) + self.m_outputSurfaceMesh.GetCellData().Modified() + self.m_outputSurfaceMesh.Modified() + + # add new attribute names to the set + self.m_newAttributeNames.add(surfaceAttributeName) + else: + self.m_logger.warning( + f"{attributeName} was skipped since it not" + + " in the input volume mesh." + ) + + return True diff --git a/geos-posp/src/geos_posp/filters/VolumeSurfaceMeshMapper.py b/geos-posp/src/geos_posp/filters/VolumeSurfaceMeshMapper.py new file mode 100644 index 00000000..8fe51316 --- /dev/null +++ b/geos-posp/src/geos_posp/filters/VolumeSurfaceMeshMapper.py @@ -0,0 +1,445 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +from typing import Optional + +import numpy as np +import numpy.typing as npt +import vtkmodules.util.numpy_support as vnp +from typing_extensions import Self +from vtk import VTK_INT # type: ignore[import-untyped] +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkIdList, + vtkInformation, + vtkInformationVector, + vtkPoints, +) +from vtkmodules.vtkCommonDataModel import vtkPolyData, vtkUnstructuredGrid + +from geos_posp.processing.ConnectionSet import ( + ConnectionSet, + ConnectionSetCollection, +) +from geos_posp.processing.geometryFunctions import getCellSideAgainstPlane +from geos_posp.utils.GeosOutputsConstants import PostProcessingOutputsEnum +from geos_posp.utils.Logger import Logger, getLogger +from geos_posp.utils.PhysicalConstants import ( + EPSILON, +) + +__doc__ = """ +VolumeSurfaceMeshMapper is a vtk filter that collects the cell of a volume mesh +adjacents to the faces of a surface mesh. + +VolumeSurfaceMeshMapper inputs are a volume mesh of type vtkUnstructuredGrid +and a surface mesh of type vtkPolyData. + +To use the filter: + +.. code-block:: python + + from filters.VolumeSurfaceMeshMapper import VolumeSurfaceMeshMapper + + # filter inputs + logger :Logger + # input objects + volumeMesh :vtkUnstructuredGrid + surfaceMesh :vtkPolyData + + # instanciate the filter + volumeSurfaceMeshMapper :VolumeSurfaceMeshMapper = VolumeSurfaceMeshMapper() + # set parameters and logger + volumeSurfaceMeshMapper.SetCreateAttribute(True) + volumeSurfaceMeshMapper.SetAttributeName("Surface1_AdjacentCell") + volumeSurfaceMeshMapper.SetLogger(logger) + # set input objects + volumeSurfaceMeshMapper.AddInputDataObject(0, volumeMesh) + volumeSurfaceMeshMapper.AddInputDataObject(1, surfaceMesh) + # do calculations + volumeSurfaceMeshMapper.Update() + # get filter output mesh (same as input volume mesh with new attribute if + # volumeSurfaceMeshMapper.SetCreateAttribute(True)) + output :vtkUnstructuredGrid = volumeSurfaceMeshMapper.GetOutputDataObject(0) + # get filter output mapping + # surface faces to volume cell mapping + surfaceToVolumeMap :dict[int, dict[int, bool]] = volumeSurfaceMeshMapper.GetSurfaceToVolumeMap() + # volume cell to surface faces mapping + volumeToSurfaceMap :dict[int, tuple[set[int], bool]] = volumeSurfaceMeshMapper.GetVolumeToSurfaceMap() +""" + + +class VolumeSurfaceMeshMapper(VTKPythonAlgorithmBase): + def __init__(self: Self) -> None: + """Vtk filter to compute cell adjacency between volume and surface meshes. + + Inputs are vtkUnstructuredGrid for volume mesh, vtkPolyData for + surface mesh, and attribute name. + + Ouputs are the volume mesh (vtkUnstructuredGrid) with a new attribute if + SetCreateAttribute was set to True, and a map of surface face indexess + as keys and adjacent volume cell indexes as values. + """ + super().__init__(nInputPorts=2, nOutputPorts=1, outputType="vtkPolyData") + + #: input volume mesh + self.m_volumeMesh: vtkUnstructuredGrid + #: input surface mesh + self.m_surfaceMesh: vtkPolyData + #: cell adjacency mapping that will be computed + # self.m_cellIdMap :dict[int, dict[int, bool]] = {} + self.m_connectionSets: ConnectionSetCollection = ConnectionSetCollection() + #: if set to True, will create an attribute in the volume mesh + self.m_createAttribute = False + #: name of the attribute to create in the volume mesh + self.m_attributeName: str = ( + PostProcessingOutputsEnum.ADJACENT_CELL_SIDE.attributeName + ) + #: logger + self.m_logger: Logger = getLogger("Volume to Surface Mapper Filter") + + def SetLogger(self: Self, logger: Logger) -> None: + """Set the logger. + + Args: + logger (Logger): logger + """ + self.m_logger = logger + + def GetAttributeName(self: Self) -> str: + """Get the name of the attribute to create. + + Returns: + str: name of the attribute. + """ + return self.m_attributeName + + def SetAttributeName(self: Self, name: str) -> None: + """Set the name of the attribute to create. + + Args: + name (str): name of the attribute. + """ + self.m_attributeName = name + + def GetCreateAttribute(self: Self) -> bool: + """Get the value of the boolean to create the attribute. + + Returns: + bool: create attribute boolean value. + """ + return self.m_createAttribute + + def SetCreateAttribute(self: Self, value: bool) -> None: + """Set the value of the boolean to create the attribute. + + Returns: + bool: True to create the attribute, False otherwise. + """ + self.m_createAttribute = value + + def GetSurfaceToVolumeConnectionSets(self: Self) -> ConnectionSetCollection: + """Get the collection of surface to volume cell ids. + + Returns: + ConnectionSetCollection: collection of ConnectionSet. + """ + return self.m_connectionSets + + def GetVolumeToSurfaceConnectionSets(self: Self) -> ConnectionSetCollection: + """Get the ConnectionSetCollection of volume to surface cell ids. + + Returns: + ConnectionSetCollection: reversed collection of connection set. + """ + return self.m_connectionSets.getReversedConnectionSetCollection() + + def RequestDataObject( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestDataObject. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + inData = self.GetInputData(inInfoVec, 0, 0) + outData = self.GetOutputData(outInfoVec, 0) + assert inData is not None + if outData is None or (not outData.IsA(inData.GetClassName())): + outData = inData.NewInstance() + outInfoVec.GetInformationObject(0).Set(outData.DATA_OBJECT(), outData) + return super().RequestDataObject(request, inInfoVec, outInfoVec) + + def FillInputPortInformation(self: Self, port: int, info: vtkInformation) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + port (int): input port + info (vtkInformationVector): info + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + if port == 0: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkUnstructuredGrid") + else: + info.Set(self.INPUT_REQUIRED_DATA_TYPE(), "vtkPolyData") + return 1 + + def RequestInformation( + self: Self, + request: vtkInformation, # noqa: F841 + inInfoVec: list[vtkInformationVector], # noqa: F841 + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestInformation. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + executive = self.GetExecutive() # noqa: F841 + outInfo = outInfoVec.GetInformationObject(0) # noqa: F841 + return 1 + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """Inherited from VTKPythonAlgorithmBase::RequestData. + + Args: + request (vtkInformation): request + inInfoVec (list[vtkInformationVector]): input objects + outInfoVec (vtkInformationVector): output objects + + Returns: + int: 1 if calculation successfully ended, 0 otherwise. + """ + try: + # input volume mesh + self.m_volumeMesh = vtkUnstructuredGrid.GetData(inInfoVec[0]) + # input surface + self.m_surfaceMesh = vtkPolyData.GetData(inInfoVec[1]) + # output volume mesh + outData: vtkUnstructuredGrid = self.GetOutputData(outInfoVec, 0) + outData.ShallowCopy(self.m_volumeMesh) + + # volume mesh properties + ptsVol: vtkPoints = self.m_volumeMesh.GetPoints() + assert ptsVol is not None, "Volume mesh points are undefined." + ptsCoordsVol: npt.NDArray[np.float64] = vnp.vtk_to_numpy(ptsVol.GetData()) + + # surface mesh properties + nbFaces: int = self.m_surfaceMesh.GetNumberOfCells() + ptsSurf: vtkPoints = self.m_surfaceMesh.GetPoints() + assert ptsSurf is not None, "Surface mesh points are undefined." + ptsCoordsSurf: npt.NDArray[np.float64] = vnp.vtk_to_numpy(ptsSurf.GetData()) + + # get cell ids for each face id + self.m_connectionSets.clear() + for faceId in range(nbFaces): + # self.m_cellIdMap[faceId] = self.getAdjacentCells( + # faceId, ptsCoordsSurf, ptsCoordsVol) + cellIdsSide: dict[int, bool] = self.getAdjacentCells( + faceId, ptsCoordsSurf, ptsCoordsVol + ) + self.m_connectionSets.add(ConnectionSet(faceId, cellIdsSide)) + + if self.m_createAttribute: + self.createAttribute(outData) + except AssertionError as e: + mess: str = "Surface to Volume mesh mapping failed due to:" + self.m_logger.error(mess) + self.m_logger.error(e, exc_info=True) + return 0 + except Exception as e: + mess0: str = "Surface to Volume mesh mapping failed due to:" + self.m_logger.critical(mess0) + self.m_logger.critical(e, exc_info=True) + return 0 + return 1 + + def getAdjacentCells( + self: Self, + faceId: int, + ptsCoordsSurf: npt.NDArray[np.float64], + ptsCoordsVol: npt.NDArray[np.float64], + ) -> dict[int, bool]: + """Get the cells from volume mesh adjacent to the face cellIdSurf. + + Args: + faceId (int): id of the face of the surface mesh. + ptsCoordsSurf (npt.NDArray[np.float64]): coordinates of the points + of the surface mesh + ptsCoordsVol (npt.NDArray[np.float64]): coordinates of the points + of the volume mesh + + Returns: + dict[int, bool]: map of cell ids adjacent to the face as keys, and + side as values + """ + # Retrieve point ids of the face of the surface + facePtIds: vtkIdList = vtkIdList() + self.m_surfaceMesh.GetCellPoints(faceId, facePtIds) + + # number of face vertices + nbPtsFace: int = facePtIds.GetNumberOfIds() + # coordinates of the vertices of the face + ptsCoordsFace: list[npt.NDArray[np.float64]] = [ + ptsCoordsSurf[facePtIds.GetId(p)] for p in range(nbPtsFace) + ] + + # get the ids of all the cells that are adjacent to the face + cellIds: set[int] = self.getCellIds(ptsCoordsFace, ptsCoordsVol) + + # get the side of each cell + cellIdsSide: dict[int, bool] = {} + for cellId in cellIds: + side: bool = self.getCellSide(cellId, faceId, ptsCoordsFace, ptsCoordsVol) + cellIdsSide[cellId] = side + + return cellIdsSide + + def getCellIds( + self: Self, + ptsCoordsFace: list[npt.NDArray[np.float64]], + ptsCoordsVol: npt.NDArray[np.float64], + ) -> set[int]: + """Get the ids of all the cells that are adjacent to input face. + + A cell is adjacent to a face if it contains all the vertices of the face. + + .. WARNING:: + Face adjacency determination relies on a geometrical test of vertex + location, it is error prone because of computational precision. + + Args: + ptsCoordsFace (npt.NDArray[np.float64]): List of vertex coordinates + of the face. The shape of the array should be (N,1). + ptsCoordsVol (npt.NDArray[np.float64]): Coodinates of the vertices + of the volume mesh. The shape of the array should be (N,M), where M + is the number of vertices in the volume mesh. + + Returns: + set[int]: set of cell ids adjacent to the face. + """ + cellIds: list[set[int]] = [] + # get the ids of the cells that contains each vertex of the face. + for coords in ptsCoordsFace: + assert coords.shape[0] == ptsCoordsVol.shape[1] + diffCoords: npt.NDArray[np.float64] = np.abs(ptsCoordsVol - coords) + idPtsVol: tuple[npt.NDArray[np.int64], ...] = np.where( + np.all(diffCoords < EPSILON, axis=-1) + ) + + assert len(idPtsVol) == 1 + idPt = idPtsVol[0] + + # In case of collocated points from the volume mesh + if len(idPt) > 1: + self.m_logger.warning( + "The volume mesh has collocated points: " + + f"{idPt}. Clean the mesh first." + ) + + # Retrieve all the cells attached to the point of the volume mesh + cellList: vtkIdList = vtkIdList() + self.m_volumeMesh.GetPointCells(idPt[0], cellList) + cellIdsVertex: set[int] = { + cellList.GetId(c) for c in range(cellList.GetNumberOfIds()) + } + cellIds += [cellIdsVertex] + # keep the cells that contain all the vertices of the face + return set.intersection(*cellIds) + + def getCellSide( + self: Self, + cellId: int, + faceId: int, + ptsCoordsFace: list[npt.NDArray[np.float64]], + ptsCoordsVol: npt.NDArray[np.float64], + ) -> bool: + """Get the side of the cell from volume mesh against the surface. + + Args: + cellId (int): cell id in the volume mesh. + faceId (int): cell id in the surface mesh. + ptsCoordsFace (list[npt.NDArray[np.float64]]): coordinates of the + vertices of the face. + ptsCoordsVol (npt.NDArray[np.float64]): coordinates of the vertices + of the cell. + + Returns: + bool: True if the cell is the same side as surface normal, False + otherwise. + """ + # Retrieve vertex coordinates of the cell of the volume mesh + cellPtIds: vtkIdList = vtkIdList() + self.m_volumeMesh.GetCellPoints(cellId, cellPtIds) + cellPtsCoords: npt.NDArray[np.float64] = np.array( + [ + ptsCoordsVol[cellPtIds.GetId(i)] + for i in range(cellPtIds.GetNumberOfIds()) + ] + ) + # get face normal vector # type: ignore[no-untyped-call] + normals: npt.NDArray[np.float64] = vnp.vtk_to_numpy( + self.m_surfaceMesh.GetCellData().GetNormals() + ) + normalVec: npt.NDArray[np.float64] = normals[faceId] + normalVec /= np.linalg.norm(normalVec) # normalization + # get cell side + return getCellSideAgainstPlane(cellPtsCoords, ptsCoordsFace[0], normalVec) + + def createAttribute(self: Self, mesh: vtkUnstructuredGrid) -> bool: + """Create the cell adjacency attribute. + + Attribute yields -1 is a cell is not adjacent to input surface, 0 if + the cell is along negative side, 1 if the cell is along positive side. + + Args: + mesh (vtkUnstructuredGrid): mesh where to add the attribute + + Returns: + bool: True if the new attribute was successfully added, + False otherwise + """ + adjacentCellIdsMap: ConnectionSetCollection = ( + self.GetVolumeToSurfaceConnectionSets() + ) + array: npt.NDArray[np.float64] = -1 * np.ones(mesh.GetNumberOfCells()) + for i in range(mesh.GetNumberOfCells()): + connectionSet: Optional[ConnectionSet] = adjacentCellIdsMap.get(i) + # cell i is not in the collection + if connectionSet is None: + continue + # get connected cell sides + values: tuple[bool, ...] = tuple( + connectionSet.getConnectedCellIds().values() + ) + # assume that all boolean values are the same, keep the first one + # convert boolean to int + array[i] = int(values[0]) + newAttr: vtkDataArray = vnp.numpy_to_vtk(array, deep=True, array_type=VTK_INT) + newAttr.SetName(self.m_attributeName) + mesh.GetCellData().AddArray(newAttr) + mesh.GetCellData().Modified() + mesh.Modified() + return True diff --git a/geos-posp/src/geos_posp/filters/__init__.py b/geos-posp/src/geos_posp/filters/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/processing/ConnectionSet.py b/geos-posp/src/geos_posp/processing/ConnectionSet.py new file mode 100644 index 00000000..d02f999a --- /dev/null +++ b/geos-posp/src/geos_posp/processing/ConnectionSet.py @@ -0,0 +1,280 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +import copy +from collections.abc import MutableSet +from typing import Iterable, Optional + +from typing_extensions import Iterator, Self + +__doc__ = """ Defines connection set and connection set collection data +structures. +""" + + +class ConnectionSet: + def __init__(self: Self, cellIdRef: int, connectedCellIds: dict[int, bool]) -> None: + """Define connection set data structure. + + A ConnectionSet stores information of connection between a reference + cell and adjacent cells. Cell information relies on unique ids, and + each connected cell is associated with a side according to connection + face normal vector. + + Args: + cellIdRef (int): reference cell id. + connectedCellIds (int): map of connected cell ids with the side. + """ + self.m_cellIdRef: int = cellIdRef + self.m_connectedCellIds: dict[int, bool] = copy.deepcopy(connectedCellIds) + + def __repr__(self: Self) -> str: + """Get the string description of the FaceConnectionSet. + + Returns: + str: string description of the FaceConnectionSet. + """ + return f"{self.m_cellIdRef} - {set(self.m_connectedCellIds.keys())}" + + def __eq__(self: Self, other: object) -> bool: + """Equality operator. + + Equality means equality of cellIdRef and equality of connected cell ids. + + Args: + other (object): another object. + + Returns: + bool: True if FaceConnectionSet are equal, False otherwise. + """ + if not isinstance(other, type(self)): + return False + + connectedCellIds1 = set(self.m_connectedCellIds.keys()) + connectedCellIds2 = set(other.m_connectedCellIds.keys()) + if len(connectedCellIds1) != len(connectedCellIds2): + return False + return (self.m_cellIdRef == other.m_cellIdRef) and all( + v1 == v2 for v1, v2 in zip(connectedCellIds1, connectedCellIds2) + ) + + def __hash__(self: Self) -> int: + """Define hash method. + + Returns: + int: hash value. + """ + return hash((self.m_cellIdRef, frozenset(self.m_connectedCellIds.keys()))) + + def getCellIdRef(self: Self) -> int: + """Get the reference cell id. + + Returns: + int: reference cell id. + """ + return self.m_cellIdRef + + def setCellIdRef(self: Self, cellIdRef: int) -> None: + """Set the reference cell id. + + Args: + cellIdRef (int): reference cell id. + """ + self.m_cellIdRef = cellIdRef + + def getConnectedCellIds(self: Self) -> dict[int, bool]: + """Get connected cell ids. + + Returns: + int: map of connected cell ids with side. + """ + return self.m_connectedCellIds + + def setConnectedCellIds(self: Self, connectedCellIds: dict[int, bool]) -> None: + """Set the connected cell ids. + + Args: + connectedCellIds (dict[int, bool]): map of connected cell ids with + side. + """ + self.m_connectedCellIds = copy.deepcopy(connectedCellIds) + + def addConnectedCells(self: Self, connectedCellsToAdd: dict[int, bool]) -> None: + """Add connected cells to the existing map of connected cells. + + The addConnectedCells() method adds element(s) to the dictionary if the + cell Id is not in the dictionary. If the cell Id is in the dictionary, + it updates the cell Id with the new side value. + + Args: + connectedCellsToAdd (dict[int, bool]): connected cells to add. + """ + self.m_connectedCellIds.update(connectedCellsToAdd) + + def copy(self: Self) -> Self: + """Create a deep copy of self. + + Returns: + ConnectionSet: copy of ConnectionSet + """ + return ConnectionSet(self.getCellIdRef(), self.getConnectedCellIds()) # type: ignore # noqa: F821 + + +class ConnectionSetCollection(MutableSet): + def __init__(self: Self) -> None: + """Define a collection of ConnectionSet. + + Because ConnectionSet relies on cell unique id, the collection imposes + uniqueness of reference cell id. + """ + self._items: set[ConnectionSet] = set() + + def __contains__(self: Self, item: object) -> bool: + """Redefine contains method. + + Args: + item (object): object to test + + Returns: + bool: True if the object is in the collection, False otherwise. + """ + if not isinstance(item, ConnectionSet): + return False + return any(obj.getCellIdRef() == item.getCellIdRef() for obj in self._items) + + def __iter__(self: Self) -> Iterator[ConnectionSet]: + """Iterator on the collection. + + Returns: + Iterator[ConnectionSet]: Iterator of ConnectionSet. + """ + return iter(self._items) + + def __len__(self: Self) -> int: + """Get the number of elements of the collection. + + Returns: + int: number of elements + """ + return len(self._items) + + def containsEqual(self: Self, item: ConnectionSet) -> bool: + """Test if a ConnectionSet is present in the collection. + + Both th reference cell id and connected cell dictionnary must match the input + ConnectionSet. + + Args: + item (ConnectionSet): ConnectionSet to add. + """ + connectionSet: Optional[ConnectionSet] = self.get(item.getCellIdRef()) + return (connectionSet is not None) and (connectionSet == item) + + def containsCellIdRef(self: Self, cellIdRef: int) -> bool: + """Test if a ConnectionSet with cellIdRef is present in the collection. + + Args: + cellIdRef (int): reference cell id + + Returns: + bool: True if a ConnectionSet is present, False otherwise. + """ + connectionSet: Optional[ConnectionSet] = self.get(cellIdRef) + return connectionSet is not None + + def add(self: Self, item: ConnectionSet) -> None: + """Add a ConnectionSet to the collection. + + Args: + item (ConnectionSet): ConnectionSet to add. + """ + assert item not in self, f"ConnectionSet {item} is already in the collection." + self._items.add(item.copy()) + + def addMultiple(self: Self, items: Iterable[ConnectionSet]) -> None: + """Add an iterable of ConnectionSet to the collection. + + Args: + items (Iterable[ConnectionSet]): list of ConnectionSet to add. + """ + for item in items: + self.add(item) + + def replace(self: Self, item: ConnectionSet) -> None: + """Replace a ConnectionSet if another one with the same cellIdRef exists. + + Args: + item (ConnectionSet): ConnectionSet to add. + """ + self.discardCellIdRef(item.getCellIdRef()) + self.add(item) + + def update(self: Self, item: ConnectionSet) -> None: + """Update or add a ConnectionSet to the collection. + + Args: + item (ConnectionSet): ConnectionSet + """ + connectionSet: Optional[ConnectionSet] = self.get(item.getCellIdRef()) + if connectionSet is None: + self.add(item) + else: + connectionSet.addConnectedCells(item.getConnectedCellIds()) + + def get(self: Self, cellIdRef: int) -> Optional[ConnectionSet]: + """Get ConnectionSet from reference cell id. + + Args: + cellIdRef (int): reference cell id + + Returns: + Optional[ConnectionSet]: ConnectionSet with cellIdRef. + """ + for connectionSet in self._items: + if connectionSet.getCellIdRef() == cellIdRef: + return connectionSet + return None + + def discard(self: Self, item: ConnectionSet) -> None: + """Remove a ConnectionSet to the collection. + + ConnectionSet is removed if both reference cell id and connected cell dictionnary + match an element of the collection. + + Args: + item (ConnectionSet): ConnectionSet to remove. + """ + self._items.discard(item) + + def discardCellIdRef(self: Self, cellIdRef: int) -> None: + """Remove a ConnectionSet to the collection using the reference cell id. + + Args: + cellIdRef (int): reference cell id to remove. + """ + item: Optional[ConnectionSet] = self.get(cellIdRef) + if item is not None: + self.discard(item) + + def __repr__(self: Self) -> str: + """Representation of ConnectionSetCollection. + + Returns: + str: representation. + """ + return f"{self.__class__.__name__}({list(self._items)})" + + def getReversedConnectionSetCollection(self: Self) -> Self: + """Get the set of reversed connection set. + + Returns: + ConnectionSetCollection: reversed collection of ConnectionSet + """ + connectionSetCollection: ConnectionSetCollection = ConnectionSetCollection() + for face2VolumeCS in self._items: + for cellId, side in face2VolumeCS.getConnectedCellIds().items(): + newConnectionSet: ConnectionSet = ConnectionSet( + cellId, {face2VolumeCS.getCellIdRef(): side} + ) + connectionSetCollection.update(newConnectionSet) + return connectionSetCollection # type: ignore # noqa: F821 diff --git a/geos-posp/src/geos_posp/processing/MohrCircle.py b/geos-posp/src/geos_posp/processing/MohrCircle.py new file mode 100644 index 00000000..5ec2cef9 --- /dev/null +++ b/geos-posp/src/geos_posp/processing/MohrCircle.py @@ -0,0 +1,119 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +import numpy as np +import numpy.typing as npt +from typing_extensions import Self + +from geos_posp.processing.geomechanicsCalculatorFunctions import ( + computeStressPrincipalComponentsFromStressVector, +) + +__doc__ = """ +MohrCircle module define the Mohr's circle parameters. + +Inputs are a 6 component stress vector, a circle id, and the mechanical +convention used for compression. +The class computes principal components from stress vector during initialization. +Accessors get access to these 3 principal components as well as circle center +and radius. + +To use the object: + +.. code-block:: python + + from processing.MohrCircle import MohrCircle + + # create the object + stressVector :npt.NDArray[np.float64] + circleId :str + mohrCircle :MohrCircle = MohrCircle(circleId) + + # either directly set principal components (p3 <= p2 <= p1) + mohrCircle.SetPrincipalComponents(p3, p2, p1) + # or compute them from stress vector + mohrCircle.computePrincipalComponents(stressVector) + + # access to members + id :str = mohrCircle.getCircleId() + p1, p2, p3 :float = mohrCircle.getPrincipalComponents() + radius :float = mohrCircle.getCircleRadius() + center :float = mohrCircle.getCircleCenter() +""" + + +class MohrCircle: + def __init__(self: Self, circleId: str) -> None: + """Compute Mohr's Circle from input stress. + + Args: + circleId (str): Mohr's circle id. + """ + self.m_circleId: str = circleId + + self.m_p1: float = 0.0 + self.m_p2: float = 0.0 + self.m_p3: float = 0.0 + + def __str__(self: Self) -> str: + """Overload of __str__ method.""" + return self.m_circleId + + def __repr__(self: Self) -> str: + """Overload of __repr__ method.""" + return self.m_circleId + + def setCircleId(self: Self, circleId: str) -> None: + """Set circle Id variable. + + Args: + circleId (str): circle Id. + """ + self.m_circleId = circleId + + def getCircleId(self: Self) -> str: + """Access the Id of the Mohr circle. + + Returns: + str: Id of the Mohr circle + """ + return self.m_circleId + + def getCircleRadius(self: Self) -> float: + """Compute and return Mohr's circle radius from principal components.""" + return (self.m_p1 - self.m_p3) / 2.0 + + def getCircleCenter(self: Self) -> float: + """Compute and return Mohr's circle center from principal components.""" + return (self.m_p1 + self.m_p3) / 2.0 + + def getPrincipalComponents(self: Self) -> tuple[float, float, float]: + """Get Moh's circle principal components.""" + return (self.m_p3, self.m_p2, self.m_p1) + + def setPrincipalComponents(self: Self, p3: float, p2: float, p1: float) -> None: + """Set principal components. + + Args: + p3 (float): first component. Must be the lowest. + p2 (float): second component. + p1 (float): third component. Must be the greatest. + """ + assert (p3 <= p2) and (p2 <= p1), "Component order is wrong." + self.m_p3 = p3 + self.m_p2 = p2 + self.m_p1 = p1 + + def computePrincipalComponents( + self: Self, stressVector: npt.NDArray[np.float64] + ) -> None: + """Calculate principal components. + + Args: + stressVector (npt.NDArray[np.float64]): 6 components stress vector + Stress vector must follow GEOS convention (XX, YY, ZZ, YZ, XZ, XY) + """ + # get stress principal components + self.m_p3, self.m_p2, self.m_p1 = ( + computeStressPrincipalComponentsFromStressVector(stressVector) + ) diff --git a/geos-posp/src/geos_posp/processing/MohrCoulomb.py b/geos-posp/src/geos_posp/processing/MohrCoulomb.py new file mode 100644 index 00000000..4072191b --- /dev/null +++ b/geos-posp/src/geos_posp/processing/MohrCoulomb.py @@ -0,0 +1,99 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +import numpy as np +import numpy.typing as npt +from typing_extensions import Self, Union + +__doc__ = """ +MohrCoulomb module define the Mohr-Coulomb failure envelop class. + +Inputs are the rock cohesion (Pa) and the friction angle (°). +2 methods allow to compute either shear stress values according to normal stress +values, or the failure envelope including normal stress and corresponding shear +stress values. + +To use the object: + +.. code-block:: python + + from processing.MohrCoulomb import MohrCoulomb + + # create the object + rockCohesion :float = 1.5e9 # Pa + frictionAngle :float = 10 # degree + mohrCoulomb = MohrCoulomb(rockCohesion, frictionAngle) + + # compute shear stress values according to normal stress values + normalStress :npt.NDArray[np.float64] = np.linspace(1e9, 1.5e9) + shearStress :npt.NDArray[np.float64] = mohrCoulomb.computeShearStress(normalStress) + + # compute the failure envelope including normal stress and corresponding shear + # stress values + # ones may also define minimum normal stress and the number of points + normalStressMax :float = 1.5e9 + normalStress, shearStress = mohrCoulomb.computeFailureEnvelop(normalStressMax) +""" + + +class MohrCoulomb: + def __init__(self: Self, rockCohesion: float, frictionAngle: float) -> None: + """Define Mohr-Coulomb failure envelop. + + Args: + rockCohesion (float): rock cohesion (Pa). + frictionAngle (float): friction angle (rad). + """ + # rock cohesion + self.m_rockCohesion = rockCohesion + # failure envelop slope + self.m_slope: float = np.tan(frictionAngle) + # intersection of failure envelop and abscissa axis + self.m_sigmaMin: float = -rockCohesion / self.m_slope + + def computeShearStress( + self: Self, stressNormal0: Union[float, npt.NDArray[np.float64]] + ) -> Union[float, npt.NDArray[np.float64]]: + """Compute shear stress from normal stress. + + Args: + stressNormal0 (float | npt.NDArray[np.float64]): normal stress + value (Pa) + + Returns: + float | npt.NDArray[np.float64]): shear stress value. + """ + stressNormal: npt.NDArray[np.float64] = np.array(stressNormal0) + tau: npt.NDArray[np.float64] = self.m_slope * stressNormal + self.m_rockCohesion + return tau + + def computeFailureEnvelop( + self: Self, + stressNormalMax: float, + stressNormalMin: Union[float, None] = None, + n: int = 100, + ) -> tuple[npt.NDArray[np.float64], npt.NDArray[np.float64]]: + """Compute the envelope failure between min and max normal stress. + + Args: + stressNormalMax (float): Maximum normal stress (Pa) + stressNormalMin (float | None, optional): Minimum normal stress. + If it is None, the envelop is computed from the its intersection + with the abscissa axis. + + Defaults to None. + n (int, optional): Number of points to define the envelop. + Defaults to 100. + + Returns: + tuple[npt.NDArray[np.float64], npt.NDArray[np.float64]]: failure + envelop coordinates where first element is the abscissa and second + element is the ordinates. + """ + sigmaMin: float = ( + self.m_sigmaMin if stressNormalMin is None else stressNormalMin + ) + stressNormal: npt.NDArray[np.float64] = np.linspace( + sigmaMin, stressNormalMax, n + ) + return (stressNormal, np.array(self.computeShearStress(stressNormal))) diff --git a/geos-posp/src/geos_posp/processing/__init__.py b/geos-posp/src/geos_posp/processing/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/processing/geomechanicsCalculatorFunctions.py b/geos-posp/src/geos_posp/processing/geomechanicsCalculatorFunctions.py new file mode 100644 index 00000000..e50cadd8 --- /dev/null +++ b/geos-posp/src/geos_posp/processing/geomechanicsCalculatorFunctions.py @@ -0,0 +1,1011 @@ +# SPDX-License-Identifier: Apache-2.0 +# # SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +import numpy as np +import numpy.typing as npt + +from geos_posp.processing.MohrCoulomb import MohrCoulomb +from geos_posp.utils.geosUtils import getAttributeMatrixFromVector +from geos_posp.utils.PhysicalConstants import ( + EPSILON, +) + +__doc__ = """Functions to compute additional geomechanical properties.""" + + +def specificGravity( + density: npt.NDArray[np.float64], specificDensity: float +) -> npt.NDArray[np.float64]: + r"""Compute the specific gravity. + + .. math:: + SG = \frac{\rho}{\rho_f} + + Args: + density (npt.NDArray[np.float64]): density (:math:`\rho` - kg/m³) + specificDensity (float): fluid density (:math:`\rho_f` - kg/m³) + + Returns: + npt.NDArray[np.float64]: specific gravity (*SG* - no unit) + + """ + assert density is not None, "Density data must be defined" + + if abs(specificDensity) < EPSILON: + return np.full_like(density, np.nan) + return density / specificDensity + + +# https://en.wikipedia.org/wiki/Elastic_modulus +def youngModulus( + bulkModulus: npt.NDArray[np.float64], shearModulus: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute Young modulus. + + .. math:: + E = \frac{9K.G}{3K+G} + + Args: + bulkModulus (npt.NDArray[np.float64]): Bulk modulus (*K* - Pa) + shearModulus (npt.NDArray[np.float64]): Shear modulus (*G* - Pa) + + Returns: + npt.NDArray[np.float64]: Young modulus (*E* - Pa) + + """ + assert bulkModulus is not None, "Bulk modulus must be defined" + assert shearModulus is not None, "Shear modulus must be defined" + # manage division by 0 by replacing with nan + assert bulkModulus.size == shearModulus.size, ( + "Bulk modulus array and Shear modulus array" + + " sizes (i.e., number of cells) must be equal." + ) + + den: npt.NDArray[np.float64] = 3.0 * bulkModulus + shearModulus + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + young: npt.NDArray[np.float64] = 9.0 * bulkModulus * shearModulus / den + young[mask] = np.nan + return young + + +def poissonRatio( + bulkModulus: npt.NDArray[np.float64], shearModulus: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute Poisson's ratio. + + .. math:: + \nu = \frac{3K-2G}{2(3K+G)} + + Args: + bulkModulus (npt.NDArray[np.float64]): Bulk modulus (*K* - Pa) + shearModulus (npt.NDArray[np.float64]): Shear modulus (*G* - Pa) + + Returns: + npt.NDArray[np.float64]: Poisson's ratio (:math:`\nu`) + + """ + assert bulkModulus is not None, "Bulk modulus must be defined" + assert shearModulus is not None, "Shear modulus must be defined" + assert bulkModulus.size == shearModulus.size, ( + "Bulk modulus array and Shear modulus array" + + " sizes (i.e., number of cells) must be equal." + ) + # manage division by 0 by replacing with nan + den: npt.NDArray[np.float64] = 2.0 * (3.0 * bulkModulus + shearModulus) + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + poisson: npt.NDArray[np.float64] = (3.0 * bulkModulus - 2.0 * shearModulus) / den + poisson[mask] = np.nan + return poisson + + +def bulkModulus( + youngModulus: npt.NDArray[np.float64], poissonRatio: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute bulk Modulus from young modulus and poisson ratio. + + .. math:: + K = \frac{E}{3(1-2\nu)} + + Args: + youngModulus (npt.NDArray[np.float64]): Young modulus (*E* - Pa) + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: Bulk modulus (*K* - Pa) + + """ + assert poissonRatio is not None, "Poisson's ratio must be defined" + assert youngModulus is not None, "Young modulus must be defined" + + den: npt.NDArray[np.float64] = 3.0 * (1.0 - 2.0 * poissonRatio) + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + bulkMod: npt.NDArray[np.float64] = youngModulus / den + bulkMod[mask] = np.nan + return bulkMod + + +def shearModulus( + youngModulus: npt.NDArray[np.float64], poissonRatio: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute shear Modulus from young modulus and poisson ratio. + + .. math:: + G = \frac{E}{2(1+\nu)} + + Args: + youngModulus (npt.NDArray[np.float64]): Young modulus (*E* - Pa) + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: Shear modulus (*G* - Pa) + + """ + assert poissonRatio is not None, "Poisson's ratio must be defined" + assert youngModulus is not None, "Young modulus must be defined" + + den: npt.NDArray[np.float64] = 2.0 * (1.0 + poissonRatio) + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + shearMod: npt.NDArray[np.float64] = youngModulus / den + shearMod[mask] = np.nan + return shearMod + + +def lambdaCoefficient( + youngModulus: npt.NDArray[np.float64], poissonRatio: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute lambda coefficient from young modulus and Poisson ratio. + + .. math:: + \lambda = \frac{E*\nu}{(1+\nu)(1-2\nu)} + + Args: + youngModulus (npt.NDArray[np.float64]): Young modulus (*E* - Pa) + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: lambda coefficient (:math:`\lambda`) + + """ + lambdaCoeff: npt.NDArray[np.float64] = poissonRatio * youngModulus + den: npt.NDArray[np.float64] = (1.0 + poissonRatio) * (1.0 - 2.0 * poissonRatio) + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + lambdaCoeff /= den + lambdaCoeff[mask] = np.nan + return lambdaCoeff + + +def oedometricModulus( + Edef: npt.NDArray[np.float64], poissonRatio: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute Oedometric modulus. + + .. math:: + M_{oed} = \frac{E_{def}}{1-2\frac{\nu^2}{1-\nu}} + + Args: + Edef (npt.NDArray[np.float64]): Deformation modulus (:math:`E_{def}` - Pa) + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: Oedometric modulus (:math:`M_{oed}` - Pa) + + """ + assert poissonRatio is not None, "Poisson's ratio must be defined" + assert Edef is not None, "Deformation modulus must be defined" + + assert Edef.size == poissonRatio.size, ( + "Deformation modulus array and Poisson's" + + " ratio array sizes (i.e., number of cells) must be equal." + ) + den: npt.NDArray[np.float64] = 1.0 - (2.0 * poissonRatio * poissonRatio) / ( + 1.0 - poissonRatio + ) + + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + EodMod: npt.NDArray[np.float64] = Edef / den + EodMod[mask] = np.nan + return EodMod + + +def biotCoefficient( + Kgrain: float, bulkModulus: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute Biot coefficient. + + .. math:: + b = 1-\frac{K}{K_{grain}} + + Args: + Kgrain (float): grain bulk modulus (:math:`K_{grain}` - Pa) + bulkModulus (npt.NDArray[np.float64]): default bulk modulus (*K* - Pa) + + Returns: + npt.NDArray[np.float64]: biot coefficient (*b*) + + """ + assert bulkModulus is not None, "Bulk modulus must be defined" + + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(Kgrain) < EPSILON + den: npt.NDArray[np.float64] = np.copy(Kgrain) + den[mask] = 1.0 + biot: npt.NDArray[np.float64] = 1.0 - bulkModulus / den + biot[mask] = np.nan + return biot + + +def totalStress( + effectiveStress: npt.NDArray[np.float64], + biot: npt.NDArray[np.float64], + pressure: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute total stress from effective stress, pressure, and Biot coeff. + + .. math:: + \sigma_{tot} = \sigma_{eff}-bP + + Args: + effectiveStress (npt.NDArray[np.float64]): effective stress + (:math:`\sigma_{eff}` - Pa) using Geos convention + biot (npt.NDArray[np.float64]): Biot coefficient (*b*) + pressure (npt.NDArray[np.float64]): Pore pressure (*P* - Pa) + + Returns: + npt.NDArray[np.float64]: total stress (:math:`\sigma_{tot}` - Pa) + + """ + assert effectiveStress is not None, "Effective stress must be defined" + assert biot is not None, "Biot coefficient must be defined" + assert pressure is not None, "Pressure must be defined" + + assert effectiveStress.shape[0] == biot.size, ( + "Biot coefficient array and " + + "effective stress sizes (i.e., number of cells) must be equal." + ) + assert biot.size == pressure.size, ( + "Biot coefficient array and pressure array" + + "sizes (i.e., number of cells) must be equal." + ) + + totalStress: npt.NDArray[np.float64] = np.copy(effectiveStress) + # pore pressure has an effect on normal stresses only + # (cf. https://dnicolasespinoza.github.io/node5.html) + nb: int = totalStress.shape[1] if totalStress.shape[1] < 4 else 3 + for j in range(nb): + totalStress[:, j] = effectiveStress[:, j] - biot * pressure + return totalStress + + +def stressRatio( + horizontalStress: npt.NDArray[np.float64], verticalStress: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute horizontal to vertical stress ratio. + + .. math:: + r = \frac{\sigma_h}{\sigma_v} + + Args: + horizontalStress (npt.NDArray[np.float64]): horizontal stress + (:math:`\sigma_h` - Pa) + verticalStress (npt.NDArray[np.float64]): vertical stress + (:math:`\sigma_v` - Pa) + + Returns: + npt.NDArray[np.float64]: stress ratio (:math:`\sigma` - Pa) + + """ + assert horizontalStress is not None, "Horizontal stress must be defined" + assert verticalStress is not None, "Vertical stress must be defined" + + assert horizontalStress.size == verticalStress.size, ( + "Horizontal stress array " + + "and vertical stress array sizes (i.e., number of cells) must be equal." + ) + + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(verticalStress) < EPSILON + verticalStress2: npt.NDArray[np.float64] = np.copy(verticalStress) + verticalStress2[mask] = 1.0 + ratio: npt.NDArray[np.float64] = horizontalStress / verticalStress2 + ratio[mask] = np.nan + return ratio + + +def lithostaticStress( + depth: npt.NDArray[np.float64], density: npt.NDArray[np.float64], gravity: float +) -> npt.NDArray[np.float64]: + """Compute the lithostatic stress. + + Args: + depth (npt.NDArray[np.float64]): depth from surface - m) + density (npt.NDArray[np.float64]): density of the overburden (kg/m³) + gravity (float): gravity (m²/s) + + Returns: + npt.NDArray[np.float64]: lithostatic stress (Pa) + + """ + # compute average density of the overburden of each point (replacing nan value by 0) + + # TODO: the formula should not depends on the density of the cell but the average + # density of the overburden. + # But how to compute the average density of the overburden in an unstructured mesh? + + # density2 = np.copy(density) + # density2[np.isnan(density)] = 0 + # overburdenMeanDensity = np.cumsum(density) / np.arange(1, density.size+1, 1) + + # TODO: which convention? + or -? + + # TODO: Warning z coordinate may be + or - if 0 is sea level. Need to take dz from surface. + # Is the surface always on top of the model? + assert depth is not None, "Depth must be defined" + assert density is not None, "Density must be defined" + + assert depth.size == density.size, ( + "Depth array " + + "and density array sizes (i.e., number of cells) must be equal." + ) + # use -1*depth to agree with Geos convention (i.e., compression with negative stress) + return -depth * density * gravity + + +def elasticStrainFromBulkShear( + deltaEffectiveStress: npt.NDArray[np.float64], + bulkModulus: npt.NDArray[np.float64], + shearModulus: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute elastic strain from Bulk and Shear moduli. + + See documentation on https://dnicolasespinoza.github.io/node5.html. + + .. math:: + \epsilon=\Delta\sigma_{eff}.C^{-1} + + + C=\begin{pmatrix} + K+\frac{4}{3}G & K-\frac{2}{3}G & K-\frac{2}{3}G & 0 & 0 & 0\\ + K-\frac{2}{3}G & K+\frac{4}{3}G & K-\frac{2}{3}G & 0 & 0 & 0\\ + K-\frac{2}{3}G & K-\frac{2}{3}G & K+\frac{4}{3}G & 0 & 0 & 0\\ + 0 & 0 & 0 & \nu & 0 & 0\\ + 0 & 0 & 0 & 0 & \nu & 0\\ + 0 & 0 & 0 & 0 & 0 & \nu\\ + \end{pmatrix} + + where *C* is stiffness tensor. + + + Args: + deltaEffectiveStress (npt.NDArray[np.float64]): effective stress + variation (:math:`\Delta\sigma_{eff}` - Pa) [S11, S22, S33, S23, S13, S12] + bulkModulus (npt.NDArray[np.float64]): Bulk modulus (*K* - Pa) + shearModulus (npt.NDArray[np.float64]): Shear modulus (*G* - Pa) + + Returns: + npt.NDArray[np.float64]: elastic strain (:math:`\epsilon`) + + """ + assert ( + deltaEffectiveStress is not None + ), "Effective stress variation must be defined" + assert bulkModulus is not None, "Bulk modulus must be defined" + assert shearModulus is not None, "Shear modulus must be defined" + + assert deltaEffectiveStress.shape[0] == bulkModulus.size, ( + "Effective stress variation " + + " and bulk modulus array sizes (i.e., number of cells) must be equal." + ) + assert shearModulus.size == bulkModulus.size, ( + "Shear modulus " + + "and bulk modulus array sizes (i.e., number of cells) must be equal." + ) + assert deltaEffectiveStress.shape[1] == 6, ( + "Effective stress variation " + "number of components must be equal to 6." + ) + + elasticStrain: npt.NDArray[np.float64] = np.full_like(deltaEffectiveStress, np.nan) + for i, stressVector in enumerate(deltaEffectiveStress): + stiffnessTensor: npt.NDArray[np.float64] = shearModulus[i] * np.identity( + 6, dtype=float + ) + for k in range(3): + for m in range(3): + val: float = ( + (bulkModulus[i] + 4.0 / 3.0 * shearModulus[i]) + if k == m + else (bulkModulus[i] - 2.0 / 3.0 * shearModulus[i]) + ) + stiffnessTensor[k, m] = val + elasticStrain[i] = stressVector @ np.linalg.inv(stiffnessTensor) + return elasticStrain + + +def elasticStrainFromYoungPoisson( + deltaEffectiveStress: npt.NDArray[np.float64], + youngModulus: npt.NDArray[np.float64], + poissonRatio: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute elastic strain from Young modulus and Poisson ratio. + + See documentation on https://dnicolasespinoza.github.io/node5.html. + + .. math:: + \epsilon=\Delta\sigma_{eff}.C^{-1} + + + C=\begin{pmatrix} + \lambda+2G & \lambda & \lambda & 0 & 0 & 0\\ + \lambda & \lambda+2G & \lambda & 0 & 0 & 0\\ + \lambda & \lambda & \lambda+2G & 0 & 0 & 0\\ + 0 & 0 & 0 & \nu & 0 & 0\\ + 0 & 0 & 0 & 0 & \nu & 0\\ + 0 & 0 & 0 & 0 & 0 & \nu\\ + \end{pmatrix} + + where *C* is stiffness tensor, :math:`\nu` is shear modulus, + :math:`\lambda` is lambda coefficient. + + Args: + deltaEffectiveStress (npt.NDArray[np.float64]): effective stress + variation (:math:`\Delta\sigma_{eff}` - Pa) [S11, S22, S33, S23, S13, S12] + youngModulus (npt.NDArray[np.float64]): Young modulus (*E* - Pa) + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: elastic strain (:math:`\epsilon`) + + """ + assert ( + deltaEffectiveStress is not None + ), "Effective stress variation must be defined" + assert youngModulus is not None, "Bulk modulus must be defined" + assert poissonRatio is not None, "Shear modulus must be defined" + + assert deltaEffectiveStress.shape[0] == youngModulus.size, ( + "Effective stress variation " + + " and bulk modulus array sizes (i.e., number of cells) must be equal." + ) + assert poissonRatio.size == youngModulus.size, ( + "Shear modulus " + + "and bulk modulus array sizes (i.e., number of cells) must be equal." + ) + assert deltaEffectiveStress.shape[1] == 6, ( + "Effective stress variation " + "number of components must be equal to 6." + ) + + # use of Lamé's equations + lambdaCoeff: npt.NDArray[np.float64] = lambdaCoefficient(youngModulus, poissonRatio) + shearMod: npt.NDArray[np.float64] = shearModulus(youngModulus, poissonRatio) + + elasticStrain: npt.NDArray[np.float64] = np.full_like(deltaEffectiveStress, np.nan) + for i, deltaStressVector in enumerate(deltaEffectiveStress): + stiffnessTensor: npt.NDArray[np.float64] = shearMod[i] * np.identity( + 6, dtype=float + ) + for k in range(3): + for m in range(3): + val: float = ( + (lambdaCoeff[i] + 2.0 * shearMod[i]) if k == m else (lambdaCoeff[i]) + ) + stiffnessTensor[k, m] = val + + elasticStrain[i] = deltaStressVector @ np.linalg.inv(stiffnessTensor) + return elasticStrain + + +def deviatoricStressPathOed( + poissonRatio: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute the Deviatoric Stress Path parameter in oedometric conditions. + + This parameter corresponds to the ratio between horizontal and vertical + stresses in oedometric conditions. + + .. math:: + DSP=\frac{\nu}{1-\nu} + + Args: + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: Deviatoric Stress Path parameter in + oedometric conditions (*DSP*) + + """ + assert poissonRatio is not None, "Poisson's ratio must be defined" + + # manage division by 0 by replacing with nan + den: npt.NDArray[np.float64] = 1 - poissonRatio + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + ratio: npt.NDArray[np.float64] = poissonRatio / den + ratio[mask] = np.nan + return ratio + + +def reservoirStressPathReal( + deltaStress: npt.NDArray[np.float64], deltaPressure: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute real reservoir stress path. + + .. math:: + RSP_{real}=\frac{\Delta\sigma}{\Delta P} + + Args: + deltaStress (npt.NDArray[np.float64]): stress difference from start + (:math:`\Delta\sigma` - Pa) + deltaPressure (npt.NDArray[np.float64]): pressure difference from start + (:math:`\Delta P` - Pa) + + Returns: + npt.NDArray[np.float64]: reservoir stress path (:math:`RSP_{real}`) + + """ + assert deltaPressure is not None, "Pressure deviation must be defined" + assert deltaStress is not None, "Stress deviation must be defined" + + assert deltaStress.shape[0] == deltaPressure.size, ( + "Total stress array and pressure variation " + + "array sizes (i.e., number of cells) must be equal." + ) + + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(deltaPressure) < EPSILON + den: npt.NDArray[np.float64] = np.copy(deltaPressure) + den[mask] = 1.0 + # use -1 to agree with Geos convention (i.e., compression with negative stress) + # take the xx, yy, and zz components only + rsp: npt.NDArray[np.float64] = np.copy(deltaStress[:, :3]) + for j in range(rsp.shape[1]): + rsp[:, j] /= den + rsp[mask, j] = np.nan + return rsp + + +def reservoirStressPathOed( + biotCoefficient: npt.NDArray[np.float64], poissonRatio: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute reservoir stress path in oedometric conditions. + + .. math:: + RSP_{oed}=b\frac{1-2\nu}{1-\nu} + + Args: + biotCoefficient (npt.NDArray[np.float64]): biot coefficient (*b*) + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`) + + Returns: + npt.NDArray[np.float64]: reservoir stress path (:math:`RSP_{oed}`) + + """ + assert biotCoefficient is not None, "Biot coefficient must be defined" + assert poissonRatio is not None, "Poisson's ratio must be defined" + + assert biotCoefficient.size == poissonRatio.size, ( + "Biot coefficient array and " + + "Poisson's ratio array sizes (i.e., number of cells) must be equal." + ) + + # manage division by 0 by replacing with nan + den: npt.NDArray[np.float64] = 1.0 - poissonRatio + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + rsp: npt.NDArray[np.float64] = biotCoefficient * (1.0 - 2.0 * poissonRatio) / den + rsp[mask] = np.nan + return rsp + + +def criticalTotalStressRatio( + pressure: npt.NDArray[np.float64], verticalStress: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute critical total stress ratio. + + Corresponds to the fracture index from Lemgruber-Traby et al (2024). + Fracturing can occur in areas where K > Total stress ratio. + (see Lemgruber-Traby, A., Cacas, M. C., Bonte, D., Rudkiewicz, J. L., Gout, C., + & Cornu, T. (2024). Basin modelling workflow applied to the screening of deep + aquifers for potential CO2 storage. Geoenergy, geoenergy2024-010. + https://doi.org/10.1144/geoenergy2024-010) + + .. math:: + \sigma_{Ĉr}=\frac{P}{\sigma_v} + + Args: + pressure (npt.NDArray[np.float64]): Pressure (*P* - Pa) + verticalStress (npt.NDArray[np.float64]): Vertical total stress + (:math:`\sigma_v` - Pa) using Geos convention + + Returns: + npt.NDArray[np.float64]: critical total stress ratio + (:math:`\sigma_{Cr}`) + + """ + assert pressure is not None, "Pressure must be defined" + assert verticalStress is not None, "Vertical stress must be defined" + + assert pressure.size == verticalStress.size, ( + "pressure array and " + + "vertical stress array sizes (i.e., number of cells) must be equal." + ) + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(verticalStress) < EPSILON + # use -1 to agree with Geos convention (i.e., compression with negative stress) + verticalStress2: npt.NDArray[np.float64] = -1.0 * np.copy(verticalStress) + verticalStress2[mask] = 1.0 + fi: npt.NDArray[np.float64] = pressure / verticalStress2 + fi[mask] = np.nan + return fi + + +def totalStressRatioThreshold( + pressure: npt.NDArray[np.float64], horizontalStress: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute total stress ratio threshold. + + Corresponds to the fracture threshold from Lemgruber-Traby et al (2024). + Fracturing can occur in areas where FT > 1. + Equals FractureIndex / totalStressRatio. + (see Lemgruber-Traby, A., Cacas, M. C., Bonte, D., Rudkiewicz, J. L., Gout, C., + & Cornu, T. (2024). Basin modelling workflow applied to the screening of deep + aquifers for potential CO2 storage. Geoenergy, geoenergy2024-010. + https://doi.org/10.1144/geoenergy2024-010) + + .. math:: + \sigma_{Th}=\frac{P}{\sigma_h} + + Args: + pressure (npt.NDArray[np.float64]): Pressure (*P* - Pa) + horizontalStress (npt.NDArray[np.float64]): minimal horizontal total + stress (:math:`\sigma_h` - Pa) using Geos convention + + Returns: + npt.NDArray[np.float64]: fracture threshold (:math:`\sigma_{Th}`) + + """ + assert pressure is not None, "Pressure must be defined" + assert horizontalStress is not None, "Horizontal stress must be defined" + + assert pressure.size == horizontalStress.size, ( + "pressure array and " + + "horizontal stress array sizes (i.e., number of cells) must be equal." + ) + + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(horizontalStress) < EPSILON + # use -1 to agree with Geos convention (i.e., compression with negative stress) + horizontalStress2: npt.NDArray[np.float64] = -1.0 * np.copy(horizontalStress) + horizontalStress2[mask] = 1.0 + ft: npt.NDArray[np.float64] = pressure / horizontalStress2 + ft[mask] = np.nan + return ft + + +def criticalPorePressure( + stressVector: npt.NDArray[np.float64], + rockCohesion: float, + frictionAngle: float = 0.0, +) -> npt.NDArray[np.float64]: + r"""Compute the critical pore pressure. + + Fracturing can occur in areas where Critical pore pressure is greater than + the pressure. + (see Khan, S., Khulief, Y., Juanes, R., Bashmal, S., Usman, M., & Al-Shuhail, A. + (2024). Geomechanical Modeling of CO2 Sequestration: A Review Focused on CO2 + Injection and Monitoring. Journal of Environmental Chemical Engineering, 112847. + https://doi.org/10.1016/j.jece.2024.112847) + + .. math:: + P_{Cr}=\frac{c.\cos(\alpha)}{1-\sin(\alpha)} + \frac{3\sigma_3-\sigma_1}{2} + + Args: + stressVector (npt.NDArray[np.float64]): stress vector + (:math:`\sigma` - Pa). + rockCohesion (float): rock cohesion (*c* - Pa) + frictionAngle (float, optional): friction angle (:math:`\alpha` - rad). + + Defaults to 0 rad. + + Returns: + npt.NDArray[np.float64]: critical pore pressure (:math:`P_{Cr}` - Pa) + + """ + assert stressVector is not None, "Stress vector must be defined" + assert stressVector.shape[1] == 6, "Stress vector must be of size 6." + + assert (frictionAngle >= 0.0) and (frictionAngle < np.pi / 2.0), ( + "Fristion angle " + "must range between 0 and pi/2." + ) + + minimumPrincipalStress: npt.NDArray[np.float64] = np.full( + stressVector.shape[0], np.nan + ) + maximumPrincipalStress: npt.NDArray[np.float64] = np.copy(minimumPrincipalStress) + for i in range(minimumPrincipalStress.shape[0]): + p3, p2, p1 = computeStressPrincipalComponentsFromStressVector(stressVector[i]) + minimumPrincipalStress[i] = p3 + maximumPrincipalStress[i] = p1 + + # assertion frictionAngle < np.pi/2., so sin(frictionAngle) != 1 + cohesiveTerm: npt.NDArray[np.float64] = ( + rockCohesion * np.cos(frictionAngle) / (1 - np.sin(frictionAngle)) + ) + residualTerm: npt.NDArray[np.float64] = ( + 3 * minimumPrincipalStress - maximumPrincipalStress + ) / 2.0 + return cohesiveTerm + residualTerm + + +def criticalPorePressureThreshold( + pressure: npt.NDArray[np.float64], criticalPorePressure: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + r"""Compute the critical pore pressure threshold. + + Defined as the ratio between pressure and critical pore pressure. + Fracturing can occur in areas where critical pore pressure threshold is >1. + + .. math:: + P_{Th}=\frac{P}{P_{Cr}} + + Args: + pressure (npt.NDArray[np.float64]): pressure (*P* - Pa) + criticalPorePressure (npt.NDArray[np.float64]): Critical pore pressure + (:math:`P_{Cr}` - Pa) + + Returns: + npt.NDArray[np.float64]: Critical pore pressure threshold (:math:`P_{Th}`) + + """ + assert pressure is not None, "Pressure must be defined" + assert criticalPorePressure is not None, "Critical pore pressure must be defined" + + assert pressure.size == criticalPorePressure.size, ( + "Pressure array and critical" + + " pore pressure array sizes (i.e., number of cells) must be equal." + ) + + # manage division by 0 by replacing with nan + mask: npt.NDArray[np.bool_] = np.abs(criticalPorePressure) < EPSILON + den = np.copy(criticalPorePressure) + den[mask] = 1.0 + index: npt.NDArray[np.float64] = pressure / den + index[mask] = np.nan + return index + + +def compressibilityOed( + shearModulus: npt.NDArray[np.float64], + bulkModulus: npt.NDArray[np.float64], + porosity: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute compressibility from elastic moduli and porosity. + + Compressibility formula is: + + .. math:: + C = \frac{1}{\phi}.\frac{3}{3K+4G} + + Args: + shearModulus (npt.NDArray[np.float64]): shear modulus (*G* - Pa). + bulkModulus (npt.NDArray[np.float64]): Bulk Modulus (*K* - Pa). + porosity (npt.NDArray[np.float64]): Rock porosity (:math:`\phi`). + + Returns: + npt.NDArray[np.float64]: Oedometric Compressibility (*C* - Pa^-1). + + """ + assert bulkModulus is not None, "Bulk modulus must be defined" + assert shearModulus is not None, "Shear modulus must be defined" + assert porosity is not None, "Porosity must be defined" + mask1: npt.NDArray[np.bool_] = np.abs(porosity) < EPSILON + den1: npt.NDArray[np.float64] = np.copy(porosity) + den1[mask1] = 1.0 + + den2: npt.NDArray[np.float64] = 3.0 * bulkModulus + 4.0 * shearModulus + mask2: npt.NDArray[np.bool_] = np.abs(den2) < EPSILON + den2[mask2] = 1.0 + + comprOed: npt.NDArray[np.float64] = 1.0 / den1 * 3.0 / den2 + comprOed[mask1] = np.nan + comprOed[mask2] = np.nan + return comprOed + + +def compressibilityReal( + deltaPressure: npt.NDArray[np.float64], + porosity: npt.NDArray[np.float64], + porosityInitial: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute compressibility from elastic moduli and porosity. + + Compressibility formula is: + + .. math:: + C = \frac{\phi-\phi_0}{\Delta P.\phi_0} + + Args: + deltaPressure (npt.NDArray[np.float64]): Pressure deviation + (:math:`\Delta P` - Pa). + porosity (npt.NDArray[np.float64]): Rock porosity (:math:`\phi`). + porosityInitial (npt.NDArray[np.float64]): initial porosity + (:math:`\phi_0`). + + Returns: + npt.NDArray[np.float64]: Real compressibility (*C* - Pa^-1). + + """ + assert deltaPressure is not None, "Pressure deviation must be defined" + assert porosity is not None, "Porosity must be defined" + assert porosityInitial is not None, "Initial porosity must be defined" + + den: npt.NDArray[np.float64] = deltaPressure * porosityInitial + mask: npt.NDArray[np.bool_] = np.abs(den) < EPSILON + den[mask] = 1.0 + + comprReal: npt.NDArray[np.float64] = (porosity - porosityInitial) / den + comprReal[mask] = np.nan + return comprReal + + +def compressibility( + poissonRatio: npt.NDArray[np.float64], + bulkModulus: npt.NDArray[np.float64], + biotCoefficient: npt.NDArray[np.float64], + porosity: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Compute compressibility from elastic moduli, biot coefficient and porosity. + + Compressibility formula is: + + .. math:: + C = \frac{1-2\nu}{\phi K}\left(\frac{b²(1+\nu)}{1-\nu} + 3(b-\phi)(1-b)\right) + + Args: + poissonRatio (npt.NDArray[np.float64]): Poisson's ratio (:math:`\nu`). + bulkModulus (npt.NDArray[np.float64]): Bulk Modulus (*K* - Pa) + biotCoefficient (npt.NDArray[np.float64]): Biot coefficient (*b*). + porosity (npt.NDArray[np.float64]): Rock porosity (:math:`\phi`). + + Returns: + npt.NDArray[np.float64]: Compressibility array (*C* - Pa^-1). + + """ + assert poissonRatio is not None, "Poisson's ratio must be defined" + assert bulkModulus is not None, "Bulk modulus must be defined" + assert biotCoefficient is not None, "Biot coefficient must be defined" + assert porosity is not None, "Porosity must be defined" + + term1: npt.NDArray[np.float64] = 1.0 - 2.0 * poissonRatio + + mask: npt.NDArray[np.bool_] = (np.abs(bulkModulus) < EPSILON) * ( + np.abs(porosity) < EPSILON + ) + denFac1: npt.NDArray[np.float64] = porosity * bulkModulus + term1[mask] = 1.0 + term1 /= denFac1 + + term2M1: npt.NDArray[np.float64] = ( + biotCoefficient * biotCoefficient * (1 + poissonRatio) + ) + denTerm2M1: npt.NDArray[np.float64] = 1 - poissonRatio + mask2: npt.NDArray[np.bool_] = np.abs(denTerm2M1) < EPSILON + denTerm2M1[mask2] = 1.0 + term2M1 /= denTerm2M1 + term2M1[mask2] = np.nan + + term2M2: npt.NDArray[np.float64] = ( + 3.0 * (biotCoefficient - porosity) * (1 - biotCoefficient) + ) + term2: npt.NDArray[np.float64] = term2M1 + term2M2 + return term1 * term2 + + +def shearCapacityUtilization( + traction: npt.NDArray[np.float64], rockCohesion: float, frictionAngle: float +) -> npt.NDArray[np.float64]: + r"""Compute shear capacity utilization (SCU). + + .. math:: + SCU = \frac{abs(\tau_1)}{\tau_{max}} + + where \tau_{max} is the Mohr-Coulomb failure threshold. + + Args: + traction (npt.NDArray[np.float64]): traction vector + (:math:`(\sigma, \tau_1, \tau2)` - Pa) + rockCohesion (float): rock cohesion (*c* - Pa). + frictionAngle (float): friction angle (:math:`\alpha` - rad). + + Returns: + npt.NDArray[np.float64]: *SCU* + + """ + assert traction is not None, "Traction must be defined" + assert traction.shape[1] == 3, "Traction vector must have 3 components." + + scu: npt.NDArray[np.float64] = np.full(traction.shape[0], np.nan) + for i, tractionVec in enumerate(traction): + # use -1 to agree with Geos convention (i.e., compression with negative stress) + stressNormal: npt.NDArray[np.float64] = -1.0 * tractionVec[0] + + # compute failure envelope + mohrCoulomb: MohrCoulomb = MohrCoulomb(rockCohesion, frictionAngle) + tauFailure: float = float(mohrCoulomb.computeShearStress(stressNormal)) + scu_i: float = np.nan + if tauFailure > 0: + scu_i = np.abs(tractionVec[1]) / tauFailure + # compute SCU + scu[i] = scu_i + return scu + + +def computeStressPrincipalComponentsFromStressVector( + stressVector: npt.NDArray[np.float64], +) -> tuple[float, float, float]: + """Compute stress principal components from stress vector. + + Args: + stressVector (npt.NDArray[np.float64]): stress vector. + + Returns: + tuple[float, float, float]: Principal components sorted in ascending + order. + + """ + assert stressVector.size == 6, "Stress vector dimension is wrong." + stressTensor: npt.NDArray[np.float64] = getAttributeMatrixFromVector(stressVector) + return computeStressPrincipalComponents(stressTensor) + + +def computeStressPrincipalComponents( + stressTensor: npt.NDArray[np.float64], +) -> tuple[float, float, float]: + """Compute stress principal components. + + Args: + stressTensor (npt.NDArray[np.float64]): stress tensor. + + Returns: + tuple[float, float, float]: Principal components sorted in ascending + order. + + """ + # get eigen values + e_val, e_vec = np.linalg.eig(stressTensor) + # sort principal stresses from smallest to largest + p3, p2, p1 = np.sort(e_val) + return (p3, p2, p1) + + +def computeNormalShearStress( + stressTensor: npt.NDArray[np.float64], directionVector: npt.NDArray[np.float64] +) -> tuple[float, float]: + """Compute normal and shear stress according to stress tensor and direction. + + Args: + stressTensor (npt.NDArray[np.float64]): 3x3 stress tensor + directionVector (npt.NDArray[np.float64]): direction vector + + Returns: + tuple[float, float]: normal and shear stresses. + + """ + assert stressTensor.shape == (3, 3), "Stress tensor must be 3x3 matrix." + assert directionVector.size == 3, "Direction vector must have 3 components" + + # normalization of direction vector + directionVector = directionVector / np.linalg.norm(directionVector) + # stress vector + T: npt.NDArray[np.float64] = np.dot(stressTensor, directionVector) + # normal stress + sigmaN: float = np.dot(T, directionVector) + # shear stress + tauVec: npt.NDArray[np.float64] = T - np.dot(sigmaN, directionVector) + tau: float = float(np.linalg.norm(tauVec)) + return (sigmaN, tau) diff --git a/geos-posp/src/geos_posp/processing/geometryFunctions.py b/geos-posp/src/geos_posp/processing/geometryFunctions.py new file mode 100644 index 00000000..0c480fd9 --- /dev/null +++ b/geos-posp/src/geos_posp/processing/geometryFunctions.py @@ -0,0 +1,155 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +import numpy as np +import numpy.typing as npt + +from geos_posp.utils.PhysicalConstants import EPSILON + +__doc__ = """Functions to permform geometry calculations.""" + + +def getChangeOfBasisMatrix( + basisFrom: tuple[ + npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64] + ], + basisTo: tuple[ + npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64] + ], +) -> npt.NDArray[np.float64]: + """Get the change of basis matrix from basis basisFrom to basis basisTo. + + Let's define the basis (basisFrom) (b1, b2, b3) and basis (basisTo) (c1, c2, c3) + where b1, b2, b3, and c1, c2, c3 are the vectors of the basis in the canonic form. + This method returns the change of basis matrix P from basisFrom to basisTo. + + The coordinates of a vector Vb(vb1, vb2, vb3) from the basis B in the basis + C is then Vc = P.Vb + + Args: + basisFrom (tuple[npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64]]): origin basis + basisTo (tuple[npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64]]): destination basis + + Returns: + npt.NDArray[np.float64]: change of basis matrix. + """ + assert (basisFrom[0].size == basisFrom[1].size) and ( + basisFrom[0].size == basisFrom[2].size + ), ("Origin " + "space vectors must have the same size.") + + assert (basisTo[0].size == basisTo[1].size) and ( + basisTo[0].size == basisTo[2].size + ), ("Destination " + "space vectors must have the same size.") + + # build the matrices where columns are the vectors of the bases + B = np.transpose(np.array(basisFrom)) + C = np.transpose(np.array(basisTo)) + # compute the inverse of C + C1: npt.NDArray[np.float64] = np.linalg.inv(C) + # get the change of basis matrix + return np.dot(C1, B) + + +def computeCoordinatesInNewBasis( + vec: npt.NDArray[np.float64], changeOfBasisMatrix: npt.NDArray[np.float64] +) -> npt.NDArray[np.float64]: + """Computes the coordinates of a matrix from a basis B in the new basis B'. + + Args: + vec (npt.NDArray[np.float64]): vector to compute the new coordinates + changeOfBasisMatrix (npt.NDArray[np.float64]): Change of basis matrix + + Returns: + npt.NDArray[np.float64]: the new coordinates of the matrix in the basis + B'. + """ + assert ( + vec.size == changeOfBasisMatrix.shape[1] + ), """The size of the vector + must be equal to the number of columns of and change of basis matrix.""" + return np.dot(changeOfBasisMatrix, vec) + + +def computePlaneFrom3Points( + pt1: npt.NDArray[np.float64], + pt2: npt.NDArray[np.float64], + pt3: npt.NDArray[np.float64], +) -> tuple[float, float, float, float]: + """Compute the 4 coefficients of a plane equation. + + Let's defined a plane from the following equation: ax + by + cz + d = 0. + This function determines a, b, c, d from 3 points of the plane. + + Args: + pt1 (npt.NDArray[np.float64]): 1st point of the plane. + pt2 (npt.NDArray[np.float64]): 2nd point of the plane. + pt3 (npt.NDArray[np.float64]): 3rd point of the plane. + + Returns: + tuple[float, float, float, float]: tuple of the 4 coefficients. + """ + # plane vectors + v1: npt.NDArray[np.float64] = pt2 - pt1 + v2: npt.NDArray[np.float64] = pt3 - pt1 + # normal vector + normal: npt.NDArray[np.float64] = np.cross(v1, v2) + assert np.linalg.norm(normal) != 0, "Vectors of the plane must not be colinear." + # first 3 coefficients of the plane equation + a, b, c = normal + # last coefficient of the plane equation + d: float = -np.dot(normal, pt1) + return a, b, c, d + + +def getCellSideAgainstPlane( + cellPtsCoords: npt.NDArray[np.float64], + planePt: npt.NDArray[np.float64], + planeNormal: npt.NDArray[np.float64], +) -> bool: + """Get the side of input cell against input plane. + + Input plane is defined by a point on it and its normal vector. + + Args: + cellPtsCoords (npt.NDArray[np.float64]): Coordinates of the vertices of + the cell to get the side. + planePt (npt.NDArray[np.float64]): Point on the plane. + planeNormal (npt.NDArray[np.float64]): Normal vector to the plane. + + Returns: + bool: True if the cell is in the direction of the normal vector, + False otherwise. + """ + assert ( + len(cellPtsCoords) > 1 + ), "The list of points must contains more than one element" + ptCenter: npt.NDArray[np.float64] = np.mean(cellPtsCoords, axis=0) + return getPointSideAgainstPlane(ptCenter, planePt, planeNormal) + + +def getPointSideAgainstPlane( + ptCoords: npt.NDArray[np.float64], + planePt: npt.NDArray[np.float64], + planeNormal: npt.NDArray[np.float64], +) -> bool: + """Get the side of input point against input plane. + + Input plane is defined by a point on it and its normal vector. + + Args: + ptCoords (npt.NDArray[np.float64]): Coordinates of the point to get + the side. + planePt (npt.NDArray[np.float64]): Point on the plane. + planeNormal (npt.NDArray[np.float64]): Normal vector to the plane. + + Returns: + bool: True if the point is in the direction of the normal vector, + False otherwise. + """ + assert ptCoords.size == 3, "Point coordinates must have 3 components" + assert planeNormal.size == 3, "Plane normal vector must have 3 components" + assert planePt.size == 3, "Plane point must have 3 components" + vec: npt.NDArray[np.float64] = ptCoords - planePt + dot: float = np.dot(planeNormal, vec) + assert abs(dot) > EPSILON, "The point is on the plane." + return dot > 0 diff --git a/geos-posp/src/geos_posp/processing/geosLogReaderFunctions.py b/geos-posp/src/geos_posp/processing/geosLogReaderFunctions.py new file mode 100644 index 00000000..fc708a3e --- /dev/null +++ b/geos-posp/src/geos_posp/processing/geosLogReaderFunctions.py @@ -0,0 +1,1048 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import contextlib +import re +from copy import deepcopy +from typing import Any, Union + +from geos_posp.utils.enumUnits import Unit, convert + +__doc__ = """Functions to read and process Geos log.""" + + +def extractRegion(geosLogLine: str) -> str: + """Extracts the name of the region from a Geos log line. + + Args: + geosLogLine (str): #expected line : "Adding Object CellElementRegion + named Reservoir from ObjectManager::Catalog." + + Raises: + ValueError: "Not enough elements to unpack in line." + ValueError: "An error has occured while parsing a line." + + + Returns: + str: "Reservoir" + """ + try: + lineElements: list[str] = geosLogLine.split() + namedElementIndex: int = lineElements.index("named") + if len(lineElements) > namedElementIndex + 1: + return lineElements[namedElementIndex + 1] + else: + raise ValueError( + "Not enough elements to unpack in region line <<" + geosLogLine + ">>" + ) + except Exception as e: + raise ValueError( + "An error has occured while parsing region line <<" + geosLogLine + ">>" + ) from e + + +def extractWell(geosLogLine: str) -> str: + """Extracts the name of the well from a Geos log line. + + Args: + geosLogLine (str): #expected line : + " TableFunction: wellControls_ConstantBHP_table" + Or + " TableFunction: wellControls_ConstantPhaseRate_table" + + Raises: + ValueError: "An error has occured while parsing <<" + geosLogLine + ">>" + + Returns: + str: "wellControls" + """ + try: + lineElements: list[str] = geosLogLine.split(":") + wellName: str = lineElements[1].replace(" ", "") + indexEndName: int + if "_ConstantBHP_table" in wellName: + indexEndName = wellName.index("_ConstantBHP_table") + elif "_ConstantPhaseRate_table" in wellName: + indexEndName = wellName.index("_ConstantPhaseRate_table") + else: + raise ValueError( + "The expected format was not found when parsing line <<" + + geosLogLine + + ">>" + ) + return wellName[:indexEndName] + except Exception as e: + raise ValueError( + "An error has occured while parsing region line <<" + geosLogLine + ">>" + ) from e + + +def extractAquifer(geosLogLine: str) -> str: + """Extracts the name of the aquifer from a Geos log line. + + Args: + geosLogLine (str): #expected line : " TableFunction: + aquifer1_pressureInfluence_table" + + Raises: + ValueError: "An error has occured while parsing <<" + + geosLogLine + + ">>" + + Returns: + str: "aquifer1" + """ + try: + lineElements: list[str] = geosLogLine.split(":") + aquiferName: str = lineElements[1].replace(" ", "") + indexEndName: int = aquiferName.index("_pressureInfluence_table") + return aquiferName[:indexEndName] + except Exception as e: + raise ValueError( + "An error has occured while parsing region line <<" + geosLogLine + ">>" + ) from e + + +def extractStatsName(geosLogLine: str) -> str: + """Extracts the name of the computed statistics name from a Geos log line. + + Args: + geosLogLine (str): #expected line :"compflowStatistics, Reservoir: + Pressure (min, average, max): 2.86419e+07, 2.93341e+07, 3.006e+07 Pa" + + Returns: + str: "compflowStatistics" + """ + lineElements: list[str] = geosLogLine.split(",") + return lineElements[0] + + +def extractPhaseModel(geosLogLine: str) -> str: + """Extracts the name of a phase model from a Geos log line. + + Args: + geosLogLine (str): #expected line : " TableFunction: + fluid_phaseModel1_PhillipsBrineDensity_table" + + Raises: + ValueError: "Not enough elements to unpack in line <<" + geosLogLine + ">>." + ValueError: "An error has occured while parsing <<" + geosLogLine + ">>" + + Returns: + str: "PhillipsBrineDensity" + """ + try: + cleanLine: str = replaceSpecialCharactersWithWhitespace(geosLogLine) + lineElements: list[str] = cleanLine.split() + phaseModels: list[str] = [elt for elt in lineElements if "phaseModel" in elt] + matchingPhaseModel: str = phaseModels[0] + phaseModelElementIndex: int = lineElements.index(matchingPhaseModel) + if len(lineElements) > phaseModelElementIndex + 1: + return lineElements[phaseModelElementIndex + 1] + else: + raise ValueError("Not enough elements to unpack in <<" + geosLogLine + ">>") + except Exception as e: + raise ValueError( + "An error has occured while parsing <<" + geosLogLine + ">>" + ) from e + + +def extractPropertiesFlow(geosLogLine: str, phasesName: list[str]) -> list[str]: + """Extracts flow property from a Geos log line. + + Args: + geosLogLine (str): #expected line : + "compflowStatistics, Reservoir: Delta pressure (min, max): 0, 0 Pa" + phasesName (list[str]): ["CO2","Water"] + + Raises: + ValueError: "Not enough elements to unpack in line <<" + geosLogLine + ">>." + ValueError: "An error has occured while parsing <<" + geosLogLine + ">>" + + Returns: + list[str]: ["Reservoir__DeltaPressureMin", "Reservoir__DeltaPressureMax"] + """ + try: + lineBlocks: list[str] = geosLogLine.split(":") + if len(lineBlocks) == 3: + propertyLineBlock: str = lineBlocks[1] + propertiesName: list[str] = buildPropertiesNameFromGeosProperties( + propertyLineBlock, phasesName + ) + statsBlock: str = lineBlocks[0] + statsElements: list[str] = statsBlock.split() + if len(statsElements) >= 2: + regionName: str = statsElements[1] + formattedRegion: str = formatPropertyName(regionName) + formattedProps = [formatPropertyName(prop) for prop in propertiesName] + propertiesFlow: list[str] = [ + formattedRegion + "__" + prop for prop in formattedProps + ] + return propertiesFlow + else: + raise ValueError( + "Incorrect number of blocks in line <<" + + geosLogLine + + ">> for it to find property name." + ) + except Exception as e: + raise ValueError( + "An error has occured while parsing <<" + geosLogLine + ">>" + ) from e + return [] + + +def buildPropertiesNameFromGeosProperties( + geosProperties: str, phasesName: list[str] +) -> list[str]: + """Extracts the property name and its extensions like min, max, average. + + Args: + geosProperties (str): " Delta pressure (min, max)" + phasesName (list[str]): ["CO2","Water"] + + Returns: + list[str]: [" Delta pressure min", " Delta pressure max"] + """ + separatedNameAndExtension: list[str] = geosProperties.split("(") + nameBlock: str = separatedNameAndExtension[0] + finalPropertiesName: list[str] = [] + if " phase " in geosProperties or " Phase " in geosProperties: + finalPropertiesName = buildPropertiesNameForPhases(nameBlock, phasesName) + elif " component " in geosProperties or " Component " in geosProperties: + finalPropertiesName = buildPropertiesNameForComponents(phasesName) + else: + # means that extensions have been found + if len(separatedNameAndExtension) == 2: + extensions: str = separatedNameAndExtension[1] + finalPropertiesName = buildPropertiesNameNoPhases(nameBlock, extensions) + else: + finalPropertiesName = buildPropertiesNameNoPhases(nameBlock) + return finalPropertiesName + + +def buildPropertiesNameForPhases(nameBlock: str, phasesName: list[str]) -> list[str]: + """Replace phase by phase names. + + Args: + nameBlock (str): " Mobile phase mass" + phasesName (list[str]): ["CO2","Water"] + + Returns: + list[str]: ['Mobile CO2 mass', 'Mobile Water mass'] + """ + propertiesName: list[str] = [] + for phaseName in phasesName: + if " phase " in nameBlock: + newName: str = nameBlock.replace("phase", phaseName) + else: + newName = nameBlock.replace("Phase", phaseName) + propertiesName.append(newName) + return propertiesName + + +def buildPropertiesNameForComponents(phasesName: list[str]) -> list[str]: + """Builds the list of component property names from the list of phases name. + + Args: + phasesName (list): ["CO2","Water"] + + Returns: + list: ['Dissolved mass CO2 in CO2','Dissolved mass Water in CO2', + 'Dissolved mass CO2 in Water','Dissolved mass Water in Water'] + """ + propertiesName: list[str] = [] + for i in range(len(phasesName)): + for j in range(len(phasesName)): + newName: str = f"Dissolved mass {phasesName[j]} in {phasesName[i]}" + propertiesName.append(newName) + return propertiesName + + +def buildPropertiesNameNoPhases(nameBlock: str, extensions: str = "") -> list[str]: + """From a name block and extensions, builds a list of properties name. + + Args: + nameBlock (str): " Delta pressure " + extensions (str): "min, max)" + + Returns: + list: [" Delta pressure min", " Delta pressure max"] + """ + if extensions != "" and "metric" not in extensions: + extensionsClean = replaceSpecialCharactersWithWhitespace(extensions) + extensionsName = extensionsClean.split() + propertiesName = [nameBlock + " " + ext for ext in extensionsName] + else: + propertiesName = [nameBlock] + return propertiesName + + +def identifyProperties(properties: list[str]) -> list[str]: + """Identify properties and add identifer. + + From a list of properties name, identifies each of them with a certain + integer, to link it to a meta property by adding an id in front of the + property name. + + Args: + properties (list[str]): ["CaprockPressureMax", "CaprockPressureMin"] + + Returns: + list[tuple[str, int]]: [1:"CaprockPressureMax", 1:"CaprockPressureMin"] + """ + idProps: list[str] = [] + # the order of the first element of every tuple is mandatory + propertiesIdentifiers: list[tuple[str, str]] = [ + ("deltapressure", "0"), + ("pressure", "1"), + ("temperature", "2"), + ("totaldynamicporevolume", "3"), + ("dynamicporevolumes", "4"), + ("nontrapped", "5"), + ("trapped", "6"), + ("immobile", "7"), + ("mobile", "8"), + ("dissolved", "9"), + ("meanbhp", "15"), + ("meantotalmassrate", "16"), + ("meantotalvolumetricrate", "17"), + ("meansurfacevolumetricrate", "18"), + ("totalmassrate", "12"), + ("totalvolumetricrate", "13"), + ("totalsurfacevolumetricrate", "13"), + ("surfacevolumetricrate", "14"), + ("totalfluidmass", "36"), + ("cellfluidmass", "37"), + ("mass", "10"), + ("bhp", "11"), + ("cumulatedvolumetricrate", "19"), + ("cumulatedvolume", "20"), + ("volumetricrate", "21"), + ("volume", "22"), + ("newtoniter", "23"), + ("lineariter", "24"), + ("stress", "25"), + ("displacement", "26"), + ("permeability", "27"), + ("porosity", "28"), + ("ratio", "29"), + ("fraction", "30"), + ("bulkmodulus", "31"), + ("shearmodulus", "32"), + ("oedometricmodulus", "33"), + ("points", "34"), + ("density", "35"), + ("time", "38"), + ("dt", "39"), + ] + for prop in properties: + identification: bool = False + for propId in propertiesIdentifiers: + if propId[0] in prop.lower(): + idProps.append(propId[1] + ":" + prop) + identification = True + break + if not identification: + raise ValueError( + f"The property <<{prop}>> could not be identified.\n" + + "Check that your list of meta properties is updated." + ) + return idProps + + +# TODO check if this function works when having more than 2 components + + +def extractValuesFlow(geosLogLine: str) -> list[float]: + """Extract values from a Geos log line. + + Args: + geosLogLine (str): Geos log line + "compflowStatistics, Reservoir: " + "Dissolved component mass: { { 0, 0 }, { 0, -6.38235e+10 } } kg" + + Returns: + list[float]: list of values in the line. + [0.0, 0.0, 0.0, -6.38235e+10] + """ + lineElements: list[str] = geosLogLine.split(":") + valuesBlock: str = lineElements[-1] + valuesBlock = valuesBlock.replace(",", " ") + valuesFound: list[float] = extractFloatsFromString(valuesBlock) + return valuesFound + + +def convertValues( + propertyNames: list[str], + propertyValues: list[float], + propertiesUnit: dict[str, Unit], +) -> list[float]: + """Convert properties to the desired units. + + Knowing two lists : 1) float numbers that are supposed to be in + SI units ; 2) properties name linked to the float numbers. + And that these lists are of same dimension, creates a new list of + float values converted to a specific unit linked to the property name. + + Args: + propertyNames (list[str]): list of property names + propertyValues (list[float]): list of property values. + propertiesUnit (dict[str, Unit]): dictionary of desired units for each + property + {"pressure": UnitPressure, ..., "propertyTypeN": UnitPropertyTypeN} + + Returns: + list[float]: list of converted values. + """ + assert len(propertyNames) == len(propertyValues) + valuesConverted: list[float] = [] + for index, name in enumerate(propertyNames): + unitObj: Unit = propertiesUnit["nounit"] + for propertyType in propertiesUnit: + if propertyType.lower() in name.lower(): + unitObj = propertiesUnit[propertyType] + break + valueConverted: float = convert(propertyValues[index], unitObj) + valuesConverted.append(valueConverted) + return valuesConverted + + +def identifyCurrentWell(geosLogLine: str, lastWellName: str) -> str: + """Identify the current name of the well rom a Geos log line. + + Because properties values of wells can be output without specifying + the name of the well which they belong to, we have to assume that + the name of well for the current properties observed is either : + + - the name of the well that can be found inside the line + - the name of the last well name found in former lines. + + Args: + geosLogLine (str): line from Geos log file + #expected lines with well name : + "Rank 18: well.CO2001: BHP (at the specified reference + elevation): 19318538.400682557 Pa" + Or + "wellControls1: BHP (at the specified reference + elevation): 12337146.157562563 Pa" + #line with no well name : + "The total rate is 0 kg/s, which corresponds to a + total surface volumetric rate of 0 sm3/s" + lastWellName (str): name of the last well found + + Raises: + ValueError: "An error has occured while parsing <>." + + Returns: + str: "wellControls" + """ + if ":" in geosLogLine: + lineElements: list[str] = geosLogLine.split(":") + if geosLogLine.startswith("Rank"): + wellName: str = lineElements[1] + else: + wellName = lineElements[0] + else: + wellName = lastWellName + wellName = wellName.lstrip().rstrip() + return wellName + + +def extractPropertiesWell(geosLogLine: str, wellName: str, phaseName: str) -> list[str]: + """Extracts the well property presented from a Geos log line. + + Args: + geosLogLine (str): "wellControls1: Phase 0 surface + volumetric rate: 30.023748128796043 sm3/s" + wellName (str): well1 + phaseName (str): phase1 + + Returns: + list[str]: ["Well1_SurfaceVolumetricRatePhase1"] + """ + wName: str = formatPropertyName(wellName) + pName: str = formatPropertyName(phaseName) + tags_association = { + "BHP": wName + "__BHP", + "total massRate": wName + "__TotalMassRate", + "total surface volumetricRate": wName + "__TotalSurfaceVolumetricRate", + "phase surface volumetricRate": wName + "__SurfaceVolumetricRate" + pName, + "well is shut": wName + "__IsShut", + "density of phase": wName + "__DensityOf" + pName, + "total fluid density": wName + "__TotalFluidDensity", + } + tags_found: list[str] = extractWellTags(geosLogLine) + propertiesWell: list[str] = [] + for tag in tags_found: + correspondingName = tags_association[tag] + propertiesWell.append(correspondingName) + return propertiesWell + + +def extractPhaseId(geosLogLine: str) -> int: + """Extracts the phase number id from a Geos log line. + + Args: + geosLogLine (str): #expected line : "wellControls1: + Phase 0 surface volumetric rate: 30.023748128796043 sm3/s" + + Raises: + ValueError: "Not enough elements to unpack in line <<" + geosLogLine + ">>." + ValueError: "An error has occured while parsing <<" + geosLogLine + ">>" + + Returns: + int: 0 + """ + try: + lineElements: list[str] = geosLogLine.lower().split() + phaseElementIndex: int = lineElements.index("phase") + if len(lineElements) > phaseElementIndex + 1: + return int(lineElements[phaseElementIndex + 1]) + else: + raise ValueError( + "Not enough elements to unpack in region line <<" + geosLogLine + ">>" + ) + except Exception as e: + raise ValueError( + "An error has occured while parsing region line <<" + geosLogLine + ">>" + ) from e + + +def extractWellTags(geosLogLine: str) -> list[str]: + """Extracts the list of well property tags available from a Geos log line. + + Args: + geosLogLine (str): line from geos log file. + + Returns: + list[str]: list of tags. + """ + if geosLogLine.startswith("Control switch"): + return [] + lower_geosLogLine = geosLogLine.lower() + tags_found_line: list[str] = [] + if "well is shut" in lower_geosLogLine: + tags_found_line.append("well is shut") + elif " bhp " in lower_geosLogLine: + tags_found_line.append("BHP") + elif "total rate" in lower_geosLogLine: + tags_found_line.append("total massRate") + if "total surface volumetric rate" in lower_geosLogLine: + tags_found_line.append("total surface volumetricRate") + elif "surface volumetric rate" in lower_geosLogLine: + tags_found_line.append("phase surface volumetricRate") + elif "density of phase" in lower_geosLogLine: + tags_found_line.append("density of phase") + elif "total fluid density" in lower_geosLogLine: + tags_found_line.append("total fluid density") + return tags_found_line + + +def extractValuesWell(geosLogLine: str, numberProperties: int) -> list[float]: + """Extract values from Geos log line and returns them as a list of floats. + + The idea here is first to extract all floats values from the line. + Now all of them are useful so we need to keep some of them. + Luckily, only the last one or two floats are useful. And to determine + that, we use the number of well properties found in the line which ranges + from one to two. + + Args: + geosLogLine (str): "Rank 129: well.CO2010: The density of + phase 0 at surface conditions is 1.86 kg/sm3." + numberProperties (int): number of well properties found in the line. + + Returns: + list[float]: value of the property. e.g. [1.86] + """ + try: + if numberProperties > 0: + valuesFound: list[float] = extractFloatsFromString(geosLogLine) + if len(valuesFound) >= numberProperties: + usefulValues: list[float] = valuesFound[-numberProperties:] + return usefulValues + else: + raise ValueError( + "Number of floats found in line is inferior to number of well properties" + + " in line <<" + + geosLogLine + + ">>." + ) + else: + raise ValueError( + "No well property found in the well property line <<" + + geosLogLine + + ">>." + ) + except Exception as e: + raise ValueError( + "Well line not corresponding to expected layering <<" + geosLogLine + ">>." + ) from e + + +def extractValueAndNameAquifer(geosLogLine: str) -> tuple[str, float]: + """Extract value and name of the aquifer contained in a Geos log line. + + Args: + geosLogLine (str): "FlowSolverBase compositionalMultiphaseFlow + (SimuDeck_aquifer_pression_meme.xml, l.28): at time 100s, the + boundary condition 'aquifer1' produces a flux of + -0.6181975187076816 kg (or moles if useMass=0)." + + Returns: + tuple[str, float]: a tuple with the name and the float value. + e.g. ("aquifer1", -0.6181975187076816) + """ + try: + lineElements: list[str] = geosLogLine.split() + indexAquifName: int = lineElements.index("produces") - 1 + indexValue: int = lineElements.index("flux") + 2 + if 0 < indexAquifName < indexValue and indexValue < len(lineElements): + aquifName: str = lineElements[indexAquifName].replace("'", "") + value: float = float(lineElements[indexValue]) + return (aquifName, value) + else: + raise ValueError( + "Aquifer name or aquifer property value is not given in the line <<" + + geosLogLine + + ">>." + ) + except Exception as e: + raise ValueError( + "Aquifer line not corresponding to expected layering <<" + + geosLogLine + + ">>." + ) from e + + +def correctZeroValuesInListOfValues(values: list[float]) -> list[float]: + """Replace orhphelin 0 values of input list. + + If 0 values are found in a list of values, either replace them with the + value found before in the list or keep it 0. We suppose that 2 zeros in a + row correspond to a continuity of the values, hence keeping it 0. + + Args: + values (list[float]): list of ints or floats + + Returns: + list[float]: list of ints or floats + """ + valuesCorrected: list[float] = deepcopy(values) + for i in range(1, len(values) - 1): + valueChecked: float = values[i] + if valueChecked == 0: + valueBefore: float = values[i - 1] + valueAfter: float = values[i + 1] + if valueBefore != 0 or valueAfter != 0: + valuesCorrected[i] = valueBefore + return valuesCorrected + + +def extractTimeAndDt(geosLogLine: str) -> tuple[float, float]: + """From a Geos log line, extracts the float values of Time and dt. + + Args: + geosLogLine (str): #expected lines : + "Time: {} years, {} days, {} hrs, {} min, {} s, dt: {} s, Cycle: {}" + "Time: {:.2f} years, dt: {} s, Cycle: {}" + "Time: {:.2f} days, dt: {} s, Cycle: {}" + "Time: {:.2f} hrs, dt: {} s, Cycle: {}" + "Time: {:.2f} min, dt: {} s, Cycle: {}" + "Time: {:4.2e} s, dt: {} s, Cycle: {}" + "Time: {]s, dt:{}s, Cycle: {}" + + Raises: + KeyError: "Cannot add time values for tag=<>" + + Returns: + tuple[float]: (time, dt) + """ + timeCounter: dict[str, float] = {"years": 0, "days": 0, "hrs": 0, "min": 0, "s": 0} + timeTag: str = "Time:" + try: + indexDT: int = geosLogLine.index("dt:") + cycleIndex: int = geosLogLine.index("Cycle:") + except ValueError: + print( + "The log line does not have valid format :\n<<" + + geosLogLine.rstrip() + + ">>\nDefault value of 0.0 returned." + ) + return (0.0, 0.0) + timePart: str = geosLogLine[len(timeTag) : indexDT] + # timePart = " {} years, {} days, {} hrs, {} min, {} s, " + timePart = timePart.replace(" ", "")[:-1] + # timePart = "{}years,{}days,{}hrs,{}min,{}s" + timeElts: list[str] = timePart.split(",") + # timeElts = ["{}years", "{}days", "{}hrs", "{}min", "{}s"] + for elt in timeElts: + lastDigitIndex: int = 0 + for i, caracter in enumerate(elt): + if caracter.isdigit(): + lastDigitIndex = i + timeValue: float = float(elt[: lastDigitIndex + 1]) + timeFactor: str = elt[lastDigitIndex + 1 :] + try: + timeCounter[timeFactor] += float(timeValue) + except KeyError: + print(f"Cannot add time values for tag=<<{timeFactor}>>") + totalTime: float = timeInSecond(timeCounter) + + dtPart: str = geosLogLine[indexDT:cycleIndex] + # dtPart = "dt: {} s, " + dtPart = dtPart.replace(" ", "")[3:-2] + # dtPart = "{}" + dt: float = float(dtPart) + return (totalTime, dt) + + +def timeInSecond(timeCounter: dict[str, float]) -> float: + """Calculates the time in s from a dict of different time quantities. + + Args: + timeCounter (dict[str, float]): timeCounter: + {"years": x0, "days": x0, "hrs": x0, "min": x0, "s": x0} + + Returns: + float: Sum in seconds of all time quantities. + """ + yearsToSeconds: float = timeCounter["years"] * 365.25 * 86400 + daysToSeconds: float = timeCounter["days"] * 86400 + hrsToSeconds: float = timeCounter["hrs"] * 3600 + minsToSeconds: float = timeCounter["min"] * 60 + s: float = timeCounter["s"] + return yearsToSeconds + daysToSeconds + hrsToSeconds + minsToSeconds + s + + +def extractNewtonIter(geosLogLine: str) -> int: + """From a Geos log line, extracts the int value of NewtonIter. + + Args: + geosLogLine (str): #expected line : + " Attempt: 0, ConfigurationIter: 0, NewtonIter: 0" + + Raises: + ValueError: "Not enough elements to unpack in time line <<" + geosLogLine + ">>." + + ValueError: "An error has occured while parsing <<" + geosLogLine + ">>" + + Returns: + int: NewtonIter + """ + try: + lineClean: str = replaceSpecialCharactersWithWhitespace(geosLogLine) + lineElements: list[str] = lineClean.split() + newtonIterIndex: int = lineElements.index("NewtonIter") + if len(lineElements) > newtonIterIndex + 1: + newtonIter: str = lineElements[newtonIterIndex + 1] + return int(newtonIter) + else: + raise ValueError( + "Not enough elements to unpack in line <<" + geosLogLine + ">>." + ) + except Exception as e: + raise ValueError( + "An error has occured while parsing <<" + geosLogLine + ">>" + ) from e + + +def extractLinearIter(geosLogLine: str) -> int: + """From a Geos log line, extracts the int value of linear iterations. + + Args: + geosLogLine (str): #expected line : + " Linear Solver | Success | Iterations: 23 | Final Rel Res: + 5.96636e-05 | Make Restrictor Time: 0 | Compute Auu Time: 0 | + SC Filter Time: 0 | Setup Time: 1.5156 s | Solve Time: 0.041093 s" + + Raises: + ValueError: "Not enough elements to unpack in time line <<" + geosLogLine + ">>." + ValueError: "An error has occured while parsing <<" + geosLogLine + ">>" + + Returns: + int: 23 + """ + try: + lineClean: str = replaceSpecialCharactersWithWhitespace(geosLogLine) + lineElements: list[str] = lineClean.split() + iterIndex: int = lineElements.index("Iterations") + if len(lineElements) > iterIndex + 1: + linearIter: str = lineElements[iterIndex + 1] + return int(linearIter) + else: + raise ValueError( + "Not enough elements to unpack in line <<" + geosLogLine + ">>." + ) + except Exception as e: + raise ValueError( + "An error has occured while parsing <<" + geosLogLine + ">>" + ) from e + + +""" +String treatments functions +""" + + +def replaceSpecialCharactersWithWhitespace(sentence: str) -> str: + """Replace every special characters in a string with whitespaces. + + Args: + sentence (str): Random string "hi '(_there(''&*$^,:;'" + + Returns: + str: "hi there " + """ + cleanSentence: str = re.sub("[^a-zA-Z0-9\n.+]", " ", sentence) + return cleanSentence + + +def formatPropertyName(propertyName: str) -> str: + """Clean the string by replacing special characters and removing spaces. + + Args: + propertyName (str): name;of:the property + + Returns: + str: NameOfTheProperty + """ + propertyClean: str = replaceSpecialCharactersWithWhitespace(propertyName) + propertyElements: list[str] = propertyClean.split() + capitalizedPropertyElements: list[str] = [ + elt[0].upper() + elt[1:] for elt in propertyElements + ] + formattedName: str = "" + for element in capitalizedPropertyElements: + formattedName += element + return formattedName + + +def extractFloatsFromString(line: str) -> list[float]: + """Extracts a list of float numbers from a string. + + Args: + line (str): A random string. + + Returns: + list[float]: [float1, ..., floatN] + """ + lineModified: str = deepcopy(line) + replacements: list[str] = ["[", "]", "{", "}"] + for replacement in replacements: + lineModified = lineModified.replace(replacement, " ") + elements: list[str] = lineModified.split() + floats: list[float] = [] + for elt in elements: + if isFloat(elt): + floats.append(float(elt)) + return floats + + +# from https://stackoverflow.com/a/20929881 +def isFloat(element: Any) -> bool: # noqa: ANN401 # disable Any error + """Check whether an element is float or not. + + Args: + element (Any): input number to test. + + Returns: + bool: True if the number is a float. + """ + if element is None: + return False + try: + float(element) + return True + except ValueError: + return False + + +def extractListIntsFromString(string: str) -> list[int]: + """Builds a list of int numbers from a string. + + Args: + string (str): A random string. + + Returns: + list[int]: [int1, ..., intN] + """ + intsFound: list[int] = [] + cleanString: str = replaceSpecialCharactersWithWhitespace(string) + lineElements: list[str] = cleanString.split() + for elt in lineElements: + with contextlib.suppress(ValueError): + intsFound.append(int(elt)) + return intsFound + + +def extractFirstIntFromString(string: str) -> int: + """Extracts the first int value from a string. + + Args: + string (str): A random string. + + Returns: + int or None if no int was found. + """ + cleanString: str = replaceSpecialCharactersWithWhitespace(string) + lineElements: list[str] = cleanString.split() + for elt in lineElements: + try: + intFound: int = int(elt) + return intFound + except ValueError: + pass + raise ValueError("Line does not contain int value.") + + +def countNumberLines(filepath: str) -> int: + """Reads a file to find the number of lines within it. + + Args: + filepath (str): Path to the file. + + Returns: + int: Number of lines in file. + """ + with open(filepath) as file: + numberLines = len(file.readlines()) + return numberLines + + +def elementsAreInLog(filepath: str, elements: list[str]) -> bool: + """Indicates if input file contains element from input list of string. + + To do so, this reads a file and checks at every line if an + element was found within the line. If an element is found, it is not + checked again. The function returns True only when there is no more + element to check. + + Args: + filepath (str): Path to the file. + elements (list[str]): Every string that needs to be find + inside the file. + + Returns: + bool: + """ + assert len(elements) > 0 + with open(filepath) as file: + for line in file: + if len(elements) == 0: + return True + for element in elements: + if element in line: + indexElement: int = elements.index(element) + elements.pop(indexElement) + break + return False + + +def findNumberPhasesSimulation(filepath: str) -> int: + """Find the number of phases from Geos log file. + + Geos logs do not have explicit message telling you how many phases + were used to perform the simulation, unlike regions, wells etc ... + Therefore, we need at least to identify the exact number of phases that + can be find in this Geos log file to extract correctly properties + regarding phase related data. + + Args: + filepath (str): Filepath to a Geos log file. + + Returns: + int: The number of phases found in the Geos log. + """ + numberLines: int = countNumberLines(filepath) + # arbitrary number of minimum lines to consider the log as readable + assert numberLines > 50 + with open(filepath) as geosFile: + line: str = geosFile.readline() + id_line: int = 1 + while not line.startswith("Time:") and id_line <= numberLines: + line = geosFile.readline() + id_line += 1 + if line.startswith("Adding Solver of type") and ( + "singlephase" in line.lower() + ): + return 1 + maxPhaseIdWell: int = -1 + while id_line <= numberLines: + line = geosFile.readline() + id_line += 1 + if "Phase mass" in line or "Phase dynamic" in line: + valuesFound: list[float] = extractValuesFlow(line) + return len(valuesFound) + lowLine: str = line.lower() + phaseTags: list[str] = [" phase ", " surface "] + if ( + all(tag in lowLine for tag in phaseTags) + and "phase surface" not in lowLine + ): + phaseIdWell: int = extractPhaseId(line) + if maxPhaseIdWell < phaseIdWell: + maxPhaseIdWell = phaseIdWell + else: + return maxPhaseIdWell + 1 + return 0 + + +def transformUserChoiceToListPhases(userChoice: Union[str, None]) -> list[str]: + """Get a list of phase name from the input string. + + When using GeosLogReader, the user can choose the names of the phases + to use. The wished format is to specify each name in the good, separated + by whitespaces or either commas. + + Args: + userChoice (str | None): Output from EnterPhaseNames string vector widget. + + Returns: + list[str]: [phase0, phase1, ..., phaseN] + """ + if userChoice is None: + return [] + choice: str = deepcopy(userChoice) + # Regular expression pattern to match any symbol that is not + # alphanumeric, comma, or whitespace + pattern = r"[^\w ,]" + matches = re.findall(pattern, userChoice) + if bool(matches): + print( + "You cannot use symbols except for commas." + + " Please separate your phase names with whitespace" + + " or with commas." + ) + return [] + choiceClean: str = choice.replace(",", " ") + phaseNames: list[str] = choiceClean.split() + return phaseNames + + +def phaseNamesBuilder(numberPhases: int, phasesFromUser: list[str]) -> list[str]: + """Build phase names. + + When creating phase names, the user can or cannot have defined his + own phase names when reading the log. Therefore, whether phase names + were provided or not, if we have N phases found in the log, a list of + N phase names will be created, starting from phase0 up to phaseN. + + Args: + numberPhases (int): Number of phases found in the log file. + phasesFromUser (list[str]): names chosen by the user, can be more + or less than numberPhases. + + Returns: + list[str]: [nameFromUser0, nameFromUser1, ..., phaseN-1, phaseN] + """ + phaseNames: list[str] = [] + size: int = len(phasesFromUser) + for i in range(numberPhases): + if i + 1 > size: + phaseNames.append("phase" + str(i)) + else: + phaseNames.append(phasesFromUser[i]) + return phaseNames diff --git a/geos-posp/src/geos_posp/processing/multiblockInpectorTreeFunctions.py b/geos-posp/src/geos_posp/processing/multiblockInpectorTreeFunctions.py new file mode 100644 index 00000000..4ad853a1 --- /dev/null +++ b/geos-posp/src/geos_posp/processing/multiblockInpectorTreeFunctions.py @@ -0,0 +1,244 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +from typing import Union, cast + +from vtkmodules.vtkCommonDataModel import ( + vtkCompositeDataSet, + vtkDataObject, + vtkDataObjectTreeIterator, + vtkMultiBlockDataSet, +) + +__doc__ = """Functions to explore and process multiblock inspector tree.""" + + +def getBlockName(input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet]) -> str: + """Get the name of input block. + + If input is a vtkMultiBlockDataSet or vtkCompositeDataSet, returns the name + of the lowest level unique child block. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block object. + + Returns: + str: name of the block in the tree. + + """ + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(input) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + blockName: str = "Block" + while iter.GetCurrentDataObject() is not None: + blockName = iter.GetCurrentMetaData().Get(vtkMultiBlockDataSet.NAME()) + block: vtkDataObject = iter.GetCurrentDataObject() + nbBlocks: int = 99 + if isinstance(block, vtkMultiBlockDataSet): + block1: vtkMultiBlockDataSet = cast(vtkMultiBlockDataSet, block) + nbBlocks = block1.GetNumberOfBlocks() + + # stop if multiple children + if nbBlocks > 1: + break + + iter.GoToNextItem() + return blockName + + +def getBlockNameFromIndex( + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], index: int +) -> str: + """Get the name of a block from input multiblock and block flat index. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block object. + index (int): flat index of the block to get the name + + Returns: + str: name of the block in the tree. + + """ + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(input) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + blockName: str = "Block" + while iter.GetCurrentDataObject() is not None: + blockName = iter.GetCurrentMetaData().Get(vtkMultiBlockDataSet.NAME()) + if iter.GetCurrentFlatIndex() == index: + break + iter.GoToNextItem() + return blockName + + +def getBlockIndexFromName( + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], name: str +) -> int: + """Get block flat index from name of node in the vtkMultiBlockDataSet tree. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block object. + name (str): name of the block to get the index in the tree. + + Returns: + int: index of the block if found, -1 otherwise. + """ + blockIndex: int = -1 + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(input) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + found: bool = False + while iter.GetCurrentDataObject() is not None: + blockName: str = iter.GetCurrentMetaData().Get(vtkMultiBlockDataSet.NAME()) + blockIndex = iter.GetCurrentFlatIndex() + if blockName.lower() == name.lower(): + found = True + break + iter.GoToNextItem() + return blockIndex if found else -1 + + +def getElementaryCompositeBlockIndexes( + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet] +) -> dict[str, int]: + """Get indexes of composite block that contains elementrary blocks. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block object. + + Returns: + dict[str, int]: dictionary that contains names as keys and flat indices + as values of the parent composite blocks of elementary blocks. + """ + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(input) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + + elementaryBlockIndexes: dict[str, int] = {} + while iter.GetCurrentDataObject() is not None: + curIndex: int = iter.GetCurrentFlatIndex() + curName: str = iter.GetCurrentMetaData().Get(vtkMultiBlockDataSet.NAME()) + curIsComposite = iter.GetCurrentDataObject().IsA("vtkMultiBlockDataSet") + iter.GoToNextItem() + nextIsNotNone = iter.GetCurrentDataObject() is not None + if ( + curIsComposite + and nextIsNotNone + and (not iter.GetCurrentDataObject().IsA("vtkMultiBlockDataSet")) + ): + elementaryBlockIndexes[curName] = curIndex + + return elementaryBlockIndexes + + +def getBlockElementIndexesFlatten( + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet] +) -> list[int]: + """Get a flatten list that contains flat indexes of elementary blocks. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block object. + + Returns: + list[int]: list of flat indexes + """ + return [i for li in getBlockElementIndexes(input) for i in li] + + +def getBlockElementIndexes( + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet] +) -> list[list[int]]: + """Get a list of list that contains flat indexes of elementary blocks. + + Each sublist contains the indexes of elementary blocks that belongs to a + same parent node. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block object. + + Returns: + list[list[int]]: list of list of flat indexes + """ + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(input) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + + blockElementIndexes: list[list[int]] = [] + indexes: list[int] = [] + while iter.GetCurrentDataObject() is not None: + curIndex: int = iter.GetCurrentFlatIndex() + if iter.GetCurrentDataObject().IsA("vtkMultiBlockDataSet"): + # change of parent node, then add the indexes of the previous + # vtkMultiBlockDataSet if needed + if len(indexes) > 0: + blockElementIndexes += [indexes] + # reinitialize the list of indexes of included blocks + indexes = [] + else: + indexes += [curIndex] + iter.GoToNextItem() + + # add the indexes of the last vtkMultiBlockDataSet if needed + if len(indexes) > 0: + blockElementIndexes += [indexes] + return blockElementIndexes + + +def getBlockFromFlatIndex( + multiBlock: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], blockIndex: int +) -> vtkDataObject: + """Get the block with blockIndex from input vtkMultiBlockDataSet. + + Args: + multiBlock (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block + blockIndex (int): block index + + Returns: + vtkMultiBlockDataSet: block if it exists, None otherwise + """ + block: vtkDataObject + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(multiBlock) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + if iter.GetCurrentFlatIndex() == blockIndex: + block = iter.GetCurrentDataObject() + break + iter.GoToNextItem() + return block + + +def getBlockFromName( + multiBlock: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], blockName: str +) -> vtkDataObject: + """Get the block named blockName from input vtkMultiBlockDataSet. + + Args: + multiBlock (vtkMultiBlockDataSet | vtkCompositeDataSet): input multi block + blockName (str): block name + + Returns: + vtkDataObject: block if it exists, None otherwise + """ + block: vtkDataObject + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(multiBlock) + iter.VisitOnlyLeavesOff() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + if iter.GetCurrentMetaData().Get(vtkMultiBlockDataSet.NAME()) == blockName: + block = vtkMultiBlockDataSet.SafeDownCast(iter.GetCurrentDataObject()) + break + iter.GoToNextItem() + return block diff --git a/geos-posp/src/geos_posp/processing/vtkUtils.py b/geos-posp/src/geos_posp/processing/vtkUtils.py new file mode 100644 index 00000000..a80d6256 --- /dev/null +++ b/geos-posp/src/geos_posp/processing/vtkUtils.py @@ -0,0 +1,1086 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +from typing import Union, cast + +import numpy as np +import numpy.typing as npt +import pandas as pd # type: ignore[import-untyped] +import vtkmodules.util.numpy_support as vnp +from vtk import ( # type: ignore[import-untyped] + VTK_CHAR, + VTK_DOUBLE, + VTK_FLOAT, + VTK_INT, + VTK_UNSIGNED_INT, +) +from vtkmodules.vtkCommonCore import ( + vtkCharArray, + vtkDataArray, + vtkDoubleArray, + vtkFloatArray, + vtkIntArray, + vtkPoints, + vtkUnsignedIntArray, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCellData, + vtkCompositeDataSet, + vtkDataObject, + vtkDataObjectTreeIterator, + vtkDataSet, + vtkMultiBlockDataSet, + vtkPlane, + vtkPointData, + vtkPointSet, + vtkPolyData, + vtkUnstructuredGrid, +) +from vtkmodules.vtkFiltersCore import ( + vtk3DLinearGridPlaneCutter, + vtkAppendDataSets, + vtkArrayRename, + vtkCellCenters, + vtkPointDataToCellData, +) +from vtkmodules.vtkFiltersExtraction import vtkExtractBlock + +from geos_posp.processing.multiblockInpectorTreeFunctions import ( + getBlockElementIndexesFlatten, + getBlockFromFlatIndex, +) + +__doc__ = """ Utilities to process vtk objects. """ + + +def getAttributeSet( + object: Union[vtkMultiBlockDataSet, vtkDataSet], onPoints: bool +) -> set[str]: + """Get the set of all attributes from an object on points or on cells. + + Args: + object (Any): object where to find the attributes. + onPoints (bool): True if attributes are on points, False if they are on + cells. + + Returns: + set[str]: set of attribute names present in input object. + """ + attributes: dict[str, int] + if isinstance(object, vtkMultiBlockDataSet): + attributes = getAttributesFromMultiBlockDataSet(object, onPoints) + elif isinstance(object, vtkDataSet): + attributes = getAttributesFromDataSet(object, onPoints) + else: + raise TypeError("Input object must be a vtkDataSet or vtkMultiBlockDataSet.") + + assert attributes is not None, "Attribute list is undefined." + + return set(attributes.keys()) if attributes is not None else set() + + +def getAttributesWithNumberOfComponents( + object: Union[vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataSet, vtkDataObject], + onPoints: bool, +) -> dict[str, int]: + """Get the dictionnary of all attributes from object on points or cells. + + Args: + object (Any): object where to find the attributes. + onPoints (bool): True if attributes are on points, False if they are on + cells. + + Returns: + dict[str, int]: dictionnary where keys are the names of the attributes + and values the number of components. + + """ + attributes: dict[str, int] + if isinstance(object, (vtkMultiBlockDataSet, vtkCompositeDataSet)): + attributes = getAttributesFromMultiBlockDataSet(object, onPoints) + elif isinstance(object, vtkDataSet): + attributes = getAttributesFromDataSet(object, onPoints) + else: + raise TypeError("Input object must be a vtkDataSet or vtkMultiBlockDataSet.") + return attributes + + +def getAttributesFromMultiBlockDataSet( + object: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], onPoints: bool +) -> dict[str, int]: + """Get the dictionnary of all attributes of object on points or on cells. + + Args: + object (vtkMultiBlockDataSet | vtkCompositeDataSet): object where to find + the attributes. + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + dict[str, int]: Dictionnary of the names of the attributes as keys, and + number of components as values. + + """ + attributes: dict[str, int] = {} + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(object) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + dataSet: vtkDataSet = vtkDataSet.SafeDownCast(iter.GetCurrentDataObject()) + blockAttributes: dict[str, int] = getAttributesFromDataSet(dataSet, onPoints) + for attributeName, nbComponents in blockAttributes.items(): + if attributeName not in attributes: + attributes[attributeName] = nbComponents + + iter.GoToNextItem() + return attributes + + +def getAttributesFromDataSet(object: vtkDataSet, onPoints: bool) -> dict[str, int]: + """Get the dictionnary of all attributes of a vtkDataSet on points or cells. + + Args: + object (vtkDataSet): object where to find the attributes. + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + dict[str, int]: List of the names of the attributes. + """ + attributes: dict[str, int] = {} + data: Union[vtkPointData, vtkCellData] + sup: str = "" + if onPoints: + data = object.GetPointData() + sup = "Point" + else: + data = object.GetCellData() + sup = "Cell" + assert data is not None, f"{sup} data was not recovered." + + nbAttributes = data.GetNumberOfArrays() + for i in range(nbAttributes): + attributeName = data.GetArrayName(i) + attribute = data.GetArray(attributeName) + assert attribute is not None, f"Attribut {attributeName} is null" + nbComponents = attribute.GetNumberOfComponents() + attributes[attributeName] = nbComponents + return attributes + + +def isAttributeInObject( + object: Union[vtkMultiBlockDataSet, vtkDataSet], attributeName: str, onPoints: bool +) -> bool: + """Check if an attribute is in the input object. + + Args: + object (vtkMultiBlockDataSet | vtkDataSet): input object + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute is in the table, False otherwise + """ + if isinstance(object, vtkMultiBlockDataSet): + return isAttributeInObjectMultiBlockDataSet(object, attributeName, onPoints) + elif isinstance(object, vtkDataSet): + return isAttributeInObjectDataSet(object, attributeName, onPoints) + else: + raise TypeError("Input object must be a vtkDataSet or vtkMultiBlockDataSet.") + + +def isAttributeInObjectMultiBlockDataSet( + object: vtkMultiBlockDataSet, attributeName: str, onPoints: bool +) -> bool: + """Check if an attribute is in the input object. + + Args: + object (vtkMultiBlockDataSet): input multiblock object + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute is in the table, False otherwise + """ + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(object) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + dataSet: vtkDataSet = vtkDataSet.SafeDownCast(iter.GetCurrentDataObject()) + if isAttributeInObjectDataSet(dataSet, attributeName, onPoints): + return True + iter.GoToNextItem() + return False + + +def isAttributeInObjectDataSet( + object: vtkDataSet, attributeName: str, onPoints: bool +) -> bool: + """Check if an attribute is in the input object. + + Args: + object (vtkDataSet): input object + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute is in the table, False otherwise + """ + data: Union[vtkPointData, vtkCellData] + sup: str = "" + if onPoints: + data = object.GetPointData() + sup = "Point" + else: + data = object.GetCellData() + sup = "Cell" + assert data is not None, f"{sup} data was not recovered." + return bool(data.HasArray(attributeName)) + + +def getArrayInObject( + object: vtkDataSet, attributeName: str, onPoints: bool +) -> npt.NDArray[np.float64]: + """Return the numpy array corresponding to input attribute name in table. + + Args: + object (PointSet or UnstructuredGrid): input object + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + ArrayLike[float]: the array corresponding to input attribute name. + """ + array: vtkDoubleArray = getVtkArrayInObject(object, attributeName, onPoints) + nparray: npt.NDArray[np.float64] = vnp.vtk_to_numpy(array) # type: ignore[no-untyped-call] + return nparray + + +def getVtkArrayInObject( + object: vtkDataSet, attributeName: str, onPoints: bool +) -> vtkDoubleArray: + """Return the array corresponding to input attribute name in table. + + Args: + object (PointSet or UnstructuredGrid): input object + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + vtkDoubleArray: the vtk array corresponding to input attribute name. + """ + array: vtkDoubleArray + assert isAttributeInObject( + object, attributeName, onPoints + ), f"{attributeName} is not in input object." + + if onPoints: + array = object.GetPointData().GetArray(attributeName) + else: + array = object.GetCellData().GetArray(attributeName) + return array + + +def getNumberOfComponents( + dataSet: Union[vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataSet], + attributeName: str, + onPoints: bool, +) -> int: + """Get the number of components of attribute attributeName in dataSet. + + Args: + dataSet (vtkMultiBlockDataSet | vtkCompositeDataSet | vtkDataSet): + dataSet where the attribute is. + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + int: number of components. + """ + if isinstance(dataSet, vtkDataSet): + return getNumberOfComponentsDataSet(dataSet, attributeName, onPoints) + elif isinstance(dataSet, (vtkMultiBlockDataSet, vtkCompositeDataSet)): + return getNumberOfComponentsMultiBlock(dataSet, attributeName, onPoints) + else: + raise AssertionError("Object type is not managed.") + + +def getNumberOfComponentsDataSet( + dataSet: vtkDataSet, attributeName: str, onPoints: bool +) -> int: + """Get the number of components of attribute attributeName in dataSet. + + Args: + dataSet (vtkDataSet): dataSet where the attribute is. + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + int: number of components. + """ + array: vtkDoubleArray = getVtkArrayInObject(dataSet, attributeName, onPoints) + return array.GetNumberOfComponents() + + +def getNumberOfComponentsMultiBlock( + dataSet: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], + attributeName: str, + onPoints: bool, +) -> int: + """Get the number of components of attribute attributeName in dataSet. + + Args: + dataSet (vtkMultiBlockDataSet | vtkCompositeDataSet): multi block data Set where the attribute is. + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + int: number of components. + """ + + elementraryBlockIndexes: list[int] = getBlockElementIndexesFlatten(dataSet) + for blockIndex in elementraryBlockIndexes: + block: vtkDataSet = cast(vtkDataSet, getBlockFromFlatIndex(dataSet, blockIndex)) + if isAttributeInObject(block, attributeName, onPoints): + array: vtkDoubleArray = getVtkArrayInObject(block, attributeName, onPoints) + return array.GetNumberOfComponents() + return 0 + + +def getComponentNames( + dataSet: Union[ + vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataSet, vtkDataObject + ], + attributeName: str, + onPoints: bool, +) -> tuple[str, ...]: + """Get the name of the components of attribute attributeName in dataSet. + + Args: + dataSet (vtkDataSet | vtkMultiBlockDataSet | vtkCompositeDataSet | vtkDataObject): dataSet + where the attribute is. + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + tuple[str,...]: names of the components. + + """ + if isinstance(dataSet, vtkDataSet): + return getComponentNamesDataSet(dataSet, attributeName, onPoints) + elif isinstance(dataSet, (vtkMultiBlockDataSet, vtkCompositeDataSet)): + return getComponentNamesMultiBlock(dataSet, attributeName, onPoints) + else: + raise AssertionError("Object type is not managed.") + + +def getComponentNamesDataSet( + dataSet: vtkDataSet, attributeName: str, onPoints: bool +) -> tuple[str, ...]: + """Get the name of the components of attribute attributeName in dataSet. + + Args: + dataSet (vtkDataSet): dataSet where the attribute is. + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + tuple[str,...]: names of the components. + + """ + array: vtkDoubleArray = getVtkArrayInObject(dataSet, attributeName, onPoints) + componentNames: list[str] = [] + if array.GetNumberOfComponents() > 1: + componentNames += [ + array.GetComponentName(i) for i in range(array.GetNumberOfComponents()) + ] + return tuple(componentNames) + + +def getComponentNamesMultiBlock( + dataSet: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], + attributeName: str, + onPoints: bool, +) -> tuple[str, ...]: + """Get the name of the components of attribute in MultiBlockDataSet. + + Args: + dataSet (vtkMultiBlockDataSet | vtkCompositeDataSet): dataSet where the + attribute is. + attributeName (str): name of the attribute + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + tuple[str,...]: names of the components. + """ + elementraryBlockIndexes: list[int] = getBlockElementIndexesFlatten(dataSet) + for blockIndex in elementraryBlockIndexes: + block: vtkDataSet = cast(vtkDataSet, getBlockFromFlatIndex(dataSet, blockIndex)) + if isAttributeInObject(block, attributeName, onPoints): + return getComponentNamesDataSet(block, attributeName, onPoints) + return () + + +def fillPartialAttributes( + multiBlockMesh: Union[vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataObject], + attributeName: str, + nbComponents: int, + onPoints: bool = False, +) -> bool: + """Fill input partial attribute of multiBlockMesh with nan values. + + Args: + multiBlockMesh (vtkMultiBlockDataSet | vtkCompositeDataSet | vtkDataObject): multiBlock + mesh where to fill the attribute + attributeName (str): attribute name + nbComponents (int): number of components + onPoints (bool, optional): Attribute is on Points (False) or + on Cells. + + Defaults to False. + + Returns: + bool: True if calculation successfully ended, False otherwise + """ + componentNames: tuple[str, ...] = () + if nbComponents > 1: + componentNames = getComponentNames(multiBlockMesh, attributeName, onPoints) + values: list[float] = [np.nan for _ in range(nbComponents)] + createConstantAttribute( + multiBlockMesh, values, attributeName, componentNames, onPoints + ) + multiBlockMesh.Modified() + return True + + +def fillAllPartialAttributes( + multiBlockMesh: Union[vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataObject], + onPoints: bool = False, +) -> bool: + """Fill all the partial attributes of multiBlockMesh with nan values. + + Args: + multiBlockMesh (vtkMultiBlockDataSet | vtkCompositeDataSet | vtkDataObject): + multiBlockMesh where to fill the attribute + onPoints (bool, optional): Attribute is on Points (False) or + on Cells. + + Defaults to False. + + Returns: + bool: True if calculation successfully ended, False otherwise + """ + attributes: dict[str, int] = getAttributesWithNumberOfComponents( + multiBlockMesh, onPoints + ) + for attributeName, nbComponents in attributes.items(): + fillPartialAttributes(multiBlockMesh, attributeName, nbComponents, onPoints) + multiBlockMesh.Modified() + return True + + +def getAttributeValuesAsDF( + surface: vtkPolyData, attributeNames: tuple[str, ...] +) -> pd.DataFrame: + """Get attribute values from input surface. + + Args: + surface (vtkPolyData): mesh where to get attribute values + attributeNames (tuple[str,...]): tuple of attribute names to get the values. + + Returns: + pd.DataFrame: DataFrame containing property names as columns. + + """ + nbRows: int = surface.GetNumberOfCells() + data: pd.DataFrame = pd.DataFrame( + np.full((nbRows, len(attributeNames)), np.nan), columns=attributeNames + ) + for attributeName in attributeNames: + if not isAttributeInObject(surface, attributeName, False): + print(f"WARNING: Attribute {attributeName} is not in the mesh.") + continue + array: npt.NDArray[np.float64] = getArrayInObject(surface, attributeName, False) + + if len(array.shape) > 1: + for i in range(array.shape[1]): + data[attributeName + f"_{i}"] = array[:, i] + data.drop( + columns=[ + attributeName, + ], + inplace=True, + ) + else: + data[attributeName] = array + return data + + +def extractBlock( + multiBlockDataSet: vtkMultiBlockDataSet, blockIndex: int +) -> vtkMultiBlockDataSet: + """Extract the block with index blockIndex from multiBlockDataSet. + + Args: + multiBlockDataSet (vtkMultiBlockDataSet): multiblock dataset from which + to extract the block + blockIndex (int): block index to extract + + Returns: + vtkMultiBlockDataSet: extracted block + """ + extractBlockfilter: vtkExtractBlock = vtkExtractBlock() + extractBlockfilter.SetInputData(multiBlockDataSet) + extractBlockfilter.AddIndex(blockIndex) + extractBlockfilter.Update() + extractedBlock: vtkMultiBlockDataSet = extractBlockfilter.GetOutput() + return extractedBlock + + +def mergeBlocks( + input: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], + keepPartialAttributes: bool = False, +) -> vtkUnstructuredGrid: + """Merge all blocks of a multi block mesh. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet ): composite + object to merge blocks + keepPartialAttributes (bool): if True, keep partial attributes after merge. + + Defaults to False. + + Returns: + vtkUnstructuredGrid: merged block object + + """ + if keepPartialAttributes: + fillAllPartialAttributes(input, False) + fillAllPartialAttributes(input, True) + + af = vtkAppendDataSets() + af.MergePointsOn() + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(input) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + block: vtkUnstructuredGrid = vtkUnstructuredGrid.SafeDownCast( + iter.GetCurrentDataObject() + ) + af.AddInputData(block) + iter.GoToNextItem() + af.Update() + return af.GetOutputDataObject(0) + + +def createEmptyAttribute( + object: vtkDataObject, + attributeName: str, + componentNames: tuple[str, ...], + dataType: int, + onPoints: bool, +) -> vtkDataArray: + """Create an empty attribute. + + Args: + object (vtkDataObject): object (vtkMultiBlockDataSet, vtkDataSet) + where to create the attribute + attributeName (str): name of the attribute + componentNames (tuple[str,...]): name of the components for vectorial + attributes + dataType (int): data type. + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute was correctly created + """ + # create empty array + newAttr: vtkDataArray + if dataType == VTK_DOUBLE: + newAttr = vtkDoubleArray() + elif dataType == VTK_FLOAT: + newAttr = vtkFloatArray() + elif dataType == VTK_INT: + newAttr = vtkIntArray() + elif dataType == VTK_UNSIGNED_INT: + newAttr = vtkUnsignedIntArray() + elif dataType == VTK_CHAR: + newAttr = vtkCharArray() + else: + raise ValueError("Attribute type is unknown.") + + newAttr.SetName(attributeName) + newAttr.SetNumberOfComponents(len(componentNames)) + if len(componentNames) > 1: + for i in range(len(componentNames)): + newAttr.SetComponentName(i, componentNames[i]) + + return newAttr + + +def createConstantAttribute( + object: Union[vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataObject], + values: list[float], + attributeName: str, + componentNames: tuple[str, ...], + onPoints: bool, +) -> bool: + """Create an attribute with a constant value everywhere if absent. + + Args: + object (vtkDataObject): object (vtkMultiBlockDataSet, vtkDataSet) + where to create the attribute + values ( list[float]): list of values of the attribute for each components + attributeName (str): name of the attribute + componentNames (tuple[str,...]): name of the components for vectorial + attributes + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute was correctly created + """ + if isinstance(object, (vtkMultiBlockDataSet, vtkCompositeDataSet)): + return createConstantAttributeMultiBlock( + object, values, attributeName, componentNames, onPoints + ) + elif isinstance(object, vtkDataSet): + listAttributes: set[str] = getAttributeSet(object, onPoints) + if attributeName not in listAttributes: + return createConstantAttributeDataSet( + object, values, attributeName, componentNames, onPoints + ) + return True + return False + + +def createConstantAttributeMultiBlock( + multiBlockDataSet: Union[vtkMultiBlockDataSet, vtkCompositeDataSet], + values: list[float], + attributeName: str, + componentNames: tuple[str, ...], + onPoints: bool, +) -> bool: + """Create an attribute with a constant value everywhere if absent. + + Args: + multiBlockDataSet (vtkMultiBlockDataSet | vtkCompositeDataSet): vtkMultiBlockDataSet + where to create the attribute + values (list[float]): list of values of the attribute for each components + attributeName (str): name of the attribute + componentNames (tuple[str,...]): name of the components for vectorial + attributes + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute was correctly created + """ + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(multiBlockDataSet) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + dataSet: vtkDataSet = vtkDataSet.SafeDownCast(iter.GetCurrentDataObject()) + listAttributes: set[str] = getAttributeSet(dataSet, onPoints) + if attributeName not in listAttributes: + createConstantAttributeDataSet( + dataSet, values, attributeName, componentNames, onPoints + ) + iter.GoToNextItem() + return True + + +def createConstantAttributeDataSet( + dataSet: vtkDataSet, + values: list[float], + attributeName: str, + componentNames: tuple[str, ...], + onPoints: bool, +) -> bool: + """Create an attribute with a constant value everywhere. + + Args: + dataSet (vtkDataSet): vtkDataSet where to create the attribute + values ( list[float]): list of values of the attribute for each components + attributeName (str): name of the attribute + componentNames (tuple[str,...]): name of the components for vectorial + attributes + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute was correctly created + """ + nbElements: int = ( + dataSet.GetNumberOfPoints() if onPoints else dataSet.GetNumberOfCells() + ) + nbComponents: int = len(values) + array: npt.NDArray[np.float64] = np.ones((nbElements, nbComponents)) + for i, val in enumerate(values): + array[:, i] *= val + createAttribute(dataSet, array, attributeName, componentNames, onPoints) + return True + + +def createAttribute( + dataSet: vtkDataSet, + array: npt.NDArray[np.float64], + attributeName: str, + componentNames: tuple[str, ...], + onPoints: bool, +) -> bool: + """Create an attribute from the given array. + + Args: + dataSet (vtkDataSet): dataSet where to create the attribute + array (npt.NDArray[np.float64]): array that contains the values + attributeName (str): name of the attribute + componentNames (tuple[str,...]): name of the components for vectorial + attributes + onPoints (bool): True if attributes are on points, False if they are + on cells. + + Returns: + bool: True if the attribute was correctly created + """ + assert isinstance( + dataSet, vtkDataSet + ), "Attribute can only be created in vtkDataSet object." + + newAttr: vtkDataArray = vnp.numpy_to_vtk(array, deep=True, array_type=VTK_DOUBLE) + newAttr.SetName(attributeName) + + nbComponents: int = newAttr.GetNumberOfComponents() + if nbComponents > 1: + for i in range(nbComponents): + newAttr.SetComponentName(i, componentNames[i]) + + if onPoints: + dataSet.GetPointData().AddArray(newAttr) + else: + dataSet.GetCellData().AddArray(newAttr) + dataSet.Modified() + return True + + +def copyAttribute( + objectFrom: vtkMultiBlockDataSet, + objectTo: vtkMultiBlockDataSet, + attributNameFrom: str, + attributNameTo: str, +) -> bool: + """Copy an attribute from objectFrom to objectTo. + + Args: + objectFrom (vtkMultiBlockDataSet): object from which to copy the attribute. + objectTo (vtkMultiBlockDataSet): object where to copy the attribute. + attributNameFrom (str): attribute name in objectFrom. + attributNameTo (str): attribute name in objectTo. + + Returns: + bool: True if copy sussfully ended, False otherwise + """ + elementaryBlockIndexesTo: list[int] = getBlockElementIndexesFlatten(objectTo) + elementaryBlockIndexesFrom: list[int] = getBlockElementIndexesFlatten(objectFrom) + + assert elementaryBlockIndexesTo == elementaryBlockIndexesFrom, ( + "ObjectFrom " + "and objectTo do not have the same block indexes." + ) + + for index in elementaryBlockIndexesTo: + # get block from initial time step object + blockT0: vtkDataSet = vtkDataSet.SafeDownCast( + getBlockFromFlatIndex(objectFrom, index) + ) + assert blockT0 is not None, "Block at intitial time step is null." + + # get block from current time step object + block: vtkDataSet = vtkDataSet.SafeDownCast( + getBlockFromFlatIndex(objectTo, index) + ) + assert block is not None, "Block at current time step is null." + try: + copyAttributeDataSet(blockT0, block, attributNameFrom, attributNameTo) + except AssertionError: + # skip attribute if not in block + continue + return True + + +def copyAttributeDataSet( + objectFrom: vtkDataSet, + objectTo: vtkDataSet, + attributNameFrom: str, + attributNameTo: str, +) -> bool: + """Copy an attribute from objectFrom to objectTo. + + Args: + objectFrom (vtkDataSet): object from which to copy the attribute. + objectTo (vtkDataSet): object where to copy the attribute. + attributNameFrom (str): attribute name in objectFrom. + attributNameTo (str): attribute name in objectTo. + + Returns: + bool: True if copy sussfully ended, False otherwise + """ + # get attribut from initial time step block + npArray: npt.NDArray[np.float64] = getArrayInObject( + objectFrom, attributNameFrom, False + ) + assert npArray is not None + componentNames: tuple[str, ...] = getComponentNames( + objectFrom, attributNameFrom, False + ) + # copy attribut to current time step block + createAttribute(objectTo, npArray, attributNameTo, componentNames, False) + objectTo.Modified() + return True + + +def renameAttribute( + object: Union[vtkMultiBlockDataSet, vtkDataSet], + attributeName: str, + newAttributeName: str, + onPoints: bool, +) -> bool: + """Rename an attribute. + + Args: + object (vtkMultiBlockDataSet): object where the attribute is + attributeName (str): name of the attribute + newAttributeName (str): new name of the attribute + onPoints (bool): True if attributes are on points, False if they are on cells. + + Returns: + bool: True if renaming operation successfully ended. + """ + if isAttributeInObject(object, attributeName, onPoints): + dim: int = int(onPoints) + filter = vtkArrayRename() + filter.SetInputData(object) + filter.SetArrayName(dim, attributeName, newAttributeName) + filter.Update() + object.ShallowCopy(filter.GetOutput()) + else: + return False + return True + + +def createCellCenterAttribute( + mesh: Union[vtkMultiBlockDataSet, vtkDataSet], cellCenterAttributeName: str +) -> bool: + """Create elementCenter attribute if it does not exist. + + Args: + mesh (vtkMultiBlockDataSet | vtkDataSet): input mesh + cellCenterAttributeName (str): Name of the attribute + + Raises: + TypeError: Raised if input mesh is not a vtkMultiBlockDataSet or a + vtkDataSet. + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + ret: int = 1 + if isinstance(mesh, vtkMultiBlockDataSet): + # initialize data object tree iterator + iter: vtkDataObjectTreeIterator = vtkDataObjectTreeIterator() + iter.SetDataSet(mesh) + iter.VisitOnlyLeavesOn() + iter.GoToFirstItem() + while iter.GetCurrentDataObject() is not None: + block: vtkDataSet = vtkDataSet.SafeDownCast(iter.GetCurrentDataObject()) + ret *= int(doCreateCellCenterAttribute(block, cellCenterAttributeName)) + iter.GoToNextItem() + elif isinstance(mesh, vtkDataSet): + ret = int(doCreateCellCenterAttribute(mesh, cellCenterAttributeName)) + else: + raise TypeError("Input object must be a vtkDataSet or vtkMultiBlockDataSet.") + return bool(ret) + + +def doCreateCellCenterAttribute( + block: vtkDataSet, cellCenterAttributeName: str +) -> bool: + """Create elementCenter attribute in a vtkDataSet if it does not exist. + + Args: + block (vtkDataSet): input mesh that must be a vtkDataSet + cellCenterAttributeName (str): Name of the attribute + + Returns: + bool: True if calculation successfully ended, False otherwise. + """ + if not isAttributeInObject(block, cellCenterAttributeName, False): + # apply ElementCenter filter + filter: vtkCellCenters = vtkCellCenters() + filter.SetInputData(block) + filter.Update() + output: vtkPointSet = filter.GetOutputDataObject(0) + assert output is not None, "vtkCellCenters output is null." + # transfer output to ouput arrays + centers: vtkPoints = output.GetPoints() + assert centers is not None, "Center are undefined." + centerCoords: vtkDataArray = centers.GetData() + assert centers is not None, "Center coordinates are undefined." + centerCoords.SetName(cellCenterAttributeName) + block.GetCellData().AddArray(centerCoords) + block.Modified() + return True + + +def computeCellCenterCoordinates(mesh: vtkDataSet) -> vtkDataArray: + """Get the coordinates of Cell center. + + Args: + mesh (vtkDataSet): input surface + + Returns: + vtkPoints: cell center coordinates + """ + assert mesh is not None, "Surface is undefined." + filter: vtkCellCenters = vtkCellCenters() + filter.SetInputDataObject(mesh) + filter.Update() + output: vtkUnstructuredGrid = filter.GetOutputDataObject(0) + assert output is not None, "Cell center output is undefined." + pts: vtkPoints = output.GetPoints() + assert pts is not None, "Cell center points are undefined." + return pts.GetData() + + +def extractSurfaceFromElevation( + mesh: vtkUnstructuredGrid, elevation: float +) -> vtkPolyData: + """Extract surface at a constant elevation from a mesh. + + Args: + mesh (vtkUnstructuredGrid): input mesh + elevation (float): elevation at which to extract the surface + + Returns: + vtkPolyData: output surface + """ + assert mesh is not None, "Input mesh is undefined." + assert isinstance(mesh, vtkUnstructuredGrid), "Wrong object type" + + bounds: tuple[float, float, float, float, float, float] = mesh.GetBounds() + ooX: float = (bounds[0] + bounds[1]) / 2.0 + ooY: float = (bounds[2] + bounds[3]) / 2.0 + + # check plane z coordinates against mesh bounds + assert (elevation <= bounds[5]) and ( + elevation >= bounds[4] + ), "Plane is out of input mesh bounds." + + plane: vtkPlane = vtkPlane() + plane.SetNormal(0.0, 0.0, 1.0) + plane.SetOrigin(ooX, ooY, elevation) + + cutter = vtk3DLinearGridPlaneCutter() + cutter.SetInputDataObject(mesh) + cutter.SetPlane(plane) + cutter.SetInterpolateAttributes(True) + cutter.Update() + return cutter.GetOutputDataObject(0) + + +def transferPointDataToCellData(mesh: vtkPointSet) -> vtkPointSet: + """Transfer point data to cell data. + + Args: + mesh (vtkPointSet): Input mesh. + + Returns: + vtkPointSet: Output mesh where point data were transferred to cells. + + """ + filter = vtkPointDataToCellData() + filter.SetInputDataObject(mesh) + filter.SetProcessAllArrays(True) + filter.Update() + return filter.GetOutputDataObject(0) + + +def getBounds( + input: Union[vtkUnstructuredGrid, vtkMultiBlockDataSet] +) -> tuple[float, float, float, float, float, float]: + """Get bounds of either single of composite data set. + + Args: + input (Union[vtkUnstructuredGrid, vtkMultiBlockDataSet]): input mesh + + Returns: + tuple[float, float, float, float, float, float]: tuple containing + bounds (xmin, xmax, ymin, ymax, zmin, zmax) + + """ + if isinstance(input, vtkMultiBlockDataSet): + return getMultiBlockBounds(input) + else: + return getMonoBlockBounds(input) + + +def getMonoBlockBounds( + input: vtkUnstructuredGrid, +) -> tuple[float, float, float, float, float, float]: + """Get boundary box extrema coordinates for a vtkUnstructuredGrid. + + Args: + input (vtkMultiBlockDataSet): input single block mesh + + Returns: + tuple[float, float, float, float, float, float]: tuple containing + bounds (xmin, xmax, ymin, ymax, zmin, zmax) + + """ + return input.GetBounds() + + +def getMultiBlockBounds( + input: vtkMultiBlockDataSet, +) -> tuple[float, float, float, float, float, float]: + """Get boundary box extrema coordinates for a vtkMultiBlockDataSet. + + Args: + input (vtkMultiBlockDataSet): input multiblock mesh + + Returns: + tuple[float, float, float, float, float, float]: bounds. + + """ + xmin, ymin, zmin = 3 * [np.inf] + xmax, ymax, zmax = 3 * [-1.0 * np.inf] + blockIndexes: list[int] = getBlockElementIndexesFlatten(input) + for blockIndex in blockIndexes: + block0: vtkDataObject = getBlockFromFlatIndex(input, blockIndex) + assert block0 is not None, "Mesh is undefined." + block: vtkDataSet = vtkDataSet.SafeDownCast(block0) + bounds: tuple[float, float, float, float, float, float] = block.GetBounds() + xmin = bounds[0] if bounds[0] < xmin else xmin + xmax = bounds[1] if bounds[1] > xmax else xmax + ymin = bounds[2] if bounds[2] < ymin else ymin + ymax = bounds[3] if bounds[3] > ymax else ymax + zmin = bounds[4] if bounds[4] < zmin else zmin + zmax = bounds[5] if bounds[5] > zmax else zmax + return xmin, xmax, ymin, ymax, zmin, zmax diff --git a/geos-posp/src/geos_posp/py.typed b/geos-posp/src/geos_posp/py.typed new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/pyvistaTools/__init__.py b/geos-posp/src/geos_posp/pyvistaTools/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/pyvistaTools/pyvistaUtils.py b/geos-posp/src/geos_posp/pyvistaTools/pyvistaUtils.py new file mode 100644 index 00000000..9849fbf1 --- /dev/null +++ b/geos-posp/src/geos_posp/pyvistaTools/pyvistaUtils.py @@ -0,0 +1,114 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +from typing import Optional, Union, cast + +import numpy as np +import numpy.typing as npt +import pandas as pd # type: ignore[import-untyped] +import pyvista as pv # type: ignore[import-not-found] +import vtkmodules.util.numpy_support as vnp +from vtkmodules.vtkCommonCore import vtkDataArray +from vtkmodules.vtkCommonDataModel import ( + vtkPolyData, +) + +import geos_posp.processing.vtkUtils as vtkUtils +from geos_posp.utils.GeosOutputsConstants import GeosDomainNameEnum + +__doc__ = r""" +This module contains utilities to process meshes using pyvista. + +""" + + +def loadDataSet( + reader: pv.PVDReader, + timeStepIndexes: list[int], + elevation: float, + properties: tuple[str], +) -> tuple[dict[str, pd.DataFrame], npt.NDArray[np.float64]]: + """Load the data using pyvista and extract properties from horizontal slice. + + Args: + reader (pv.PVDReader): pyvista pvd reader + timeStepIndexes (list[int]): list of time step indexes to load. + elevation (float): elevation (m) of horizontal slice + properties (tuple[str]): list of properties to extract + + Returns: + tuple[dict[str, pd.DataFrame], npt.NDArray[np.float64]]: tuple containing + a dictionnary with times as keys and dataframe with properties as + values, and an array with cell center coordinates of the slice. + + """ + timeToPropertyMap: dict[str, pd.DataFrame] = {} + surface: vtkPolyData + timeValues: list[float] = reader.time_values + for index in timeStepIndexes: + assert index < len(timeValues), "Time step index is out of range." + + time: float = timeValues[index] + reader.set_active_time_value(time) + inputMesh: pv.Multiblock = reader.read() + + volMesh: Optional[Union[pv.MultiBlock, pv.UnstructuredGrid]] = getBlockByName( + inputMesh, GeosDomainNameEnum.VOLUME_DOMAIN_NAME.value + ) + assert volMesh is not None, "Volumic mesh was not found." + + # Merge volume block + mergedMesh: pv.UnstructuredGrid + if isinstance(volMesh, pv.MultiBlock): + mergedMesh = volMesh.combine(merge_points=True) + else: + mergedMesh = volMesh + + assert mergedMesh is not None, "Merged mesh is undefined." + + # extract data + surface = vtkUtils.extractSurfaceFromElevation(mergedMesh, elevation) + # transfer point data to cell center + surface = cast(vtkPolyData, vtkUtils.transferPointDataToCellData(surface)) + timeToPropertyMap[str(time)] = vtkUtils.getAttributeValuesAsDF( + surface, properties + ) + + # get cell center coordinates + assert surface is not None, "Surface are undefined." + pointsCoords: vtkDataArray = vtkUtils.computeCellCenterCoordinates(surface) + assert pointsCoords is not None, "Cell center are undefined." + pointsCoordsNp: npt.NDArray[np.float64] = vnp.vtk_to_numpy(pointsCoords) + return (timeToPropertyMap, pointsCoordsNp) + + +def getBlockByName( + multiBlockMesh: Union[pv.MultiBlock, pv.UnstructuredGrid], blockName: str +) -> Optional[Union[pv.MultiBlock, pv.UnstructuredGrid]]: + """Get a block in a multi block mesh from its name. + + Args: + multiBlockMesh (Union[pv.MultiBlock, pv.UnstructuredGrid]): input mesh + blockName (str): name of the block + + Returns: + Optional[Union[pv.MultiBlock, pv.UnstructuredGrid]]: wanted block if it + was found + + """ + if isinstance(multiBlockMesh, pv.UnstructuredGrid): + return None + + mesh: Optional[Union[pv.MultiBlock, pv.UnstructuredGrid]] + for i, mbMesh in enumerate(multiBlockMesh): + # if one of the block of multiBlockMesh is the volumic mesh, + # then save the mesh and break + if multiBlockMesh.get_block_name(i) == blockName: + mesh = mbMesh + break + # else look at its internal mesh(es) + mesh = getBlockByName(mbMesh, blockName) + # if mesh is not None, it is the searched one + if mesh is not None: + break + return mesh diff --git a/geos-posp/src/geos_posp/readers/GeosLogReaderAquifers.py b/geos-posp/src/geos_posp/readers/GeosLogReaderAquifers.py new file mode 100644 index 00000000..d1ed0a88 --- /dev/null +++ b/geos-posp/src/geos_posp/readers/GeosLogReaderAquifers.py @@ -0,0 +1,179 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +from io import TextIOBase + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +import geos_posp.processing.geosLogReaderFunctions as fcts +from geos_posp.utils.enumUnits import Unit + + +class GeosLogReaderAquifers: + def __init__(self: Self, filepath: str, propertiesUnit: dict[str, Unit]) -> None: + """Reader for Aquifer. + + Args: + filepath (str): path to geos log file. + propertiesUnit ( dict[str, Unit]): unit preferences + """ + self.m_propertiesUnit = propertiesUnit + self.m_aquiferNames: list[str] = [] + self.m_aquifersPropertiesValues: dict[str, list[float]] = {} + self.m_timesteps: list[float] = [] + + toFindInLog: list[str] = ["_pressureInfluence_table", "Time: 0"] + if not fcts.elementsAreInLog(filepath, toFindInLog): + print( + "Invalid Geos log file. Please check that your log" + + " did not crash and contains aquifers." + ) + else: + self.readAll(filepath) + self.calculateExtraValues() + + def readAquiferNames(self: Self, file: TextIOBase) -> tuple[str, int]: + """Initialize the m_aquiferNames attribute by reading log file. + + Args: + file (TextIOBase): Geos Log file + + Returns: + tuple(str, int): The last line with time info read. + The id of the last line read that contained the tag "_pressureInfluence_table"., + which will be the line containing the first positive timestep at 0s. + """ + aquiferNames: list[str] = [] + line: str = file.readline() + id_line = 1 + while not line.startswith("Time: 0"): + if "_pressureInfluence_table" in line: + aquiferName: str = fcts.extractAquifer(line) + aquiferNames.append(aquiferName) + line = file.readline() + id_line += 1 + self.m_aquiferNames = aquiferNames + return (line, id_line) + + def readPropertiesValues( + self: Self, file: TextIOBase, line: str, id_line: int, total_lines: int + ) -> None: + """Read aquifer property values from geos log file. + + Initialize the m_aquifersPropertiesValues and m_timesteps attributes by reading + the Geos log. If a timestep contains the tag m_computeStatisticsName, the + current timestep is added to m_timesteps and we recover the property values + in m_regionsPropertiesValues. + + Args: + file (TextIOBase): Geos Log file + line (str): last line read in the file. + id_line (int): The id of the last line read in readPhaseNames. + total_lines (int): The number of lines in the file. + """ + aquifsPropertiesValues: dict[str, list[float]] = {} + for aquifName in self.m_aquiferNames: + propVolume: str = aquifName + "__Volume" + propVolumeId: str = fcts.identifyProperties([propVolume])[0] + propRate: str = aquifName + "__VolumetricRate" + propRateId: str = fcts.identifyProperties([propRate])[0] + aquifsPropertiesValues[propVolumeId] = [0.0] + aquifsPropertiesValues[propRateId] = [0.0] + newTimestep, currentDT = fcts.extractTimeAndDt(line) + timesteps: list[float] = [newTimestep] + line = file.readline() + id_line += 1 + while id_line <= total_lines: + if line.startswith("Time:"): + newTimestep, currentDT = fcts.extractTimeAndDt(line) + newTimestep = fcts.convertValues( + ["Time"], [newTimestep], self.m_propertiesUnit + )[0] + if " produces a flux of " in line: + if newTimestep not in timesteps and newTimestep > max( + timesteps, default=0.0 + ): + timesteps.append(newTimestep) + for key in aquifsPropertiesValues: + aquifsPropertiesValues[key].append(0.0) + aquifName, volume = fcts.extractValueAndNameAquifer(line) + rate: float = volume / currentDT + propVol: str = aquifName + "__Volume" + propVolId: str = fcts.identifyProperties([propVol])[0] + propRate = aquifName + "__VolumetricRate" + propRateId = fcts.identifyProperties([propRate])[0] + aquifsPropertiesValues[propVolId][-1] = fcts.convertValues( + [propVol], [volume], self.m_propertiesUnit + )[0] + aquifsPropertiesValues[propRateId][-1] = fcts.convertValues( + [propRate], [rate], self.m_propertiesUnit + )[0] + line = file.readline() + id_line += 1 + self.m_aquifersPropertiesValues = aquifsPropertiesValues + self.m_timesteps = timesteps + + def readAll(self: Self, filepath: str) -> None: + """Initialize all the attributes of the class by reading a Geos log file. + + Args: + filepath (str): Geos log filepath. + """ + with open(filepath) as geosFile: + total_lines: int = fcts.countNumberLines(filepath) + line, id_line = self.readAquiferNames(geosFile) + self.readPropertiesValues(geosFile, line, id_line, total_lines) + + def calculateExtraValues(self: Self) -> None: + """Add cumulated columns for each aquifer volume and aquifer rate.""" + for aquifName in self.m_aquiferNames: + propVolume: str = aquifName + "__Volume" + propVolumeId: str = fcts.identifyProperties([propVolume])[0] + propRate: str = aquifName + "__VolumetricRate" + propRateId: str = fcts.identifyProperties([propRate])[0] + volumes: list[float] = self.m_aquifersPropertiesValues[propVolumeId] + rates: list[float] = self.m_aquifersPropertiesValues[propRateId] + cumuVol_name = aquifName + "__CumulatedVolume" + cumuVolId: str = fcts.identifyProperties([cumuVol_name])[0] + cumuRate_name = aquifName + "__CumulatedVolumetricRate" + cumuRateId: str = fcts.identifyProperties([cumuRate_name])[0] + cumuVol_values: list[float] = [volumes[0]] + cumuRate_values: list[float] = [rates[0]] + for i in range(1, len(volumes)): + cumuVol_values.append(cumuVol_values[i - 1] + volumes[i]) + cumuRate_values.append(cumuRate_values[i - 1] + rates[i]) + self.m_aquifersPropertiesValues[cumuVolId] = cumuVol_values + self.m_aquifersPropertiesValues[cumuRateId] = cumuRate_values + + def createDataframe(self: Self) -> pd.DataFrame: + """Create and fill and return dataframeAquifers. + + Returns: + pd.DataFrame: dataframe with values from Geos log. + """ + try: + colNames: list[str] = [] + colValues: list[float] = [] + for propName, values in self.m_aquifersPropertiesValues.items(): + unitObj: Unit = self.m_propertiesUnit["nounit"] + for propertyType in self.m_propertiesUnit: + if propertyType.lower() in propName.lower(): + unitObj = self.m_propertiesUnit[propertyType] + break + if unitObj.unitLabel == "": + raise ValueError( + "No unit was found for this property name <<" + propName + ">>." + ) + columnName: str = propName + "__" + unitObj.unitLabel + colNames.append(columnName) + colValues.append(values) # type: ignore[arg-type] + timeUnit: Unit = self.m_propertiesUnit["time"] + timeName: str = "Time__" + timeUnit.unitLabel + colNames.append(timeName) + colValues.append(self.m_timesteps) # type: ignore[arg-type] + data = {colNames[i]: colValues[i] for i in range(len(colNames))} + dataframeAquifers: pd.DataFrame = pd.DataFrame(data) + return dataframeAquifers + except ValueError as err: + print(err.args[0]) diff --git a/geos-posp/src/geos_posp/readers/GeosLogReaderConvergence.py b/geos-posp/src/geos_posp/readers/GeosLogReaderConvergence.py new file mode 100644 index 00000000..50abc432 --- /dev/null +++ b/geos-posp/src/geos_posp/readers/GeosLogReaderConvergence.py @@ -0,0 +1,131 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +from io import TextIOBase + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +import geos_posp.processing.geosLogReaderFunctions as fcts +from geos_posp.utils.enumUnits import Unit + + +class GeosLogReaderConvergence: + def __init__(self: Self, filepath: str, propertiesUnit: dict[str, Unit]) -> None: + """Reader for Convergence information. + + Args: + filepath (str): path to geos log file. + propertiesUnit ( dict[str, Unit]): unit preferences + """ + self.m_propertiesUnit: dict[str, Unit] = propertiesUnit + self.m_solversIterationsValues: dict[str, list[float]] = {} + self.m_timesteps: list[float] = [] + self.m_dts: list[float] = [] + + toFindInLog: list[str] = ["Time:"] + if not fcts.elementsAreInLog(filepath, toFindInLog): + print("Invalid Geos log file. Please check that your log did not crash.") + else: + self.readAll(filepath) + self.calculateExtraValues() + + def readIterationsValues(self: Self, file: TextIOBase, total_lines: int) -> None: + """Read iteration values from Geos log file. + + Initialize the m_aquifersPropertiesValues and m_timesteps attributes + by reading the Geos log. If a timestep contains the tag + m_computeStatisticsName, the current timestep is added to m_timesteps + and we recover the property values in m_regionsPropertiesValues. + + Args: + file (TextIOBase): Geos Log file + total_lines (int): The number of lines in the file. + """ + newtonIterId, linearIterId = fcts.identifyProperties( + ["NewtonIter", "LinearIter"] + ) + iterationsValues: dict[str, list[float]] = {newtonIterId: [], linearIterId: []} + timesteps: list[float] = [] + dts: list[float] = [] + line: str = file.readline() + id_line = 1 + while not line.startswith("Time:"): + line = file.readline() + id_line += 1 + while id_line <= total_lines: + if line.startswith("Time:"): + timestep, dt = fcts.extractTimeAndDt(line) + timestep, dt = fcts.convertValues( + ["Time", "Time"], [timestep, dt], self.m_propertiesUnit + ) + if timestep > max(timesteps, default=-9.9e99): + timesteps.append(timestep) + dts.append(dt) + iterationsValues[newtonIterId].append(0.0) + iterationsValues[linearIterId].append(0.0) + elif "NewtonIter:" in line: + newtonIter: int = fcts.extractNewtonIter(line) + if newtonIter > 0: + iterationsValues[newtonIterId][-1] += 1.0 + elif "Linear Solver" in line: + linearIter: int = fcts.extractLinearIter(line) + iterationsValues[linearIterId][-1] += linearIter + line = file.readline() + id_line += 1 + self.m_solversIterationsValues = iterationsValues + self.m_timesteps = timesteps + self.m_dts = dts + + def readAll(self: Self, filepath: str) -> None: + """Initialize all the attributes of the class by reading a Geos log file. + + Args: + filepath (str): Geos log filepath. + """ + with open(filepath) as geosFile: + total_lines: int = fcts.countNumberLines(filepath) + self.readIterationsValues(geosFile, total_lines) + + def calculateExtraValues(self: Self) -> None: + """Add cumulated columns for newtonIter and linearIter.""" + siv: dict[str, list[float]] = self.m_solversIterationsValues + cumulatedNewtonIter, cumulatedLinearIter = fcts.identifyProperties( + ["CumulatedNewtonIter", "CumulatedLinearIter"] + ) + siv[cumulatedNewtonIter] = [] + siv[cumulatedLinearIter] = [] + newtonIterId, linearIterId = fcts.identifyProperties( + ["NewtonIter", "LinearIter"] + ) + newtonIter: list[float] = siv[newtonIterId] + linearIter: list[float] = siv[linearIterId] + sumNewtonIter: float = 0.0 + sumLinearIter: float = 0.0 + for i in range(len(newtonIter)): + sumNewtonIter += newtonIter[i] + sumLinearIter += linearIter[i] + siv[cumulatedNewtonIter].append(sumNewtonIter) + siv[cumulatedLinearIter].append(sumLinearIter) + + def createDataframe(self: Self) -> pd.DataFrame: + """Create and fill and return dataframeSolversIterations. + + Returns: + pd.DataFrame: dataframe with values from Geos log. + """ + colNames: list[str] = [] + colValues: list[float] = [] + for propName, values in self.m_solversIterationsValues.items(): + colNames.append(propName) + colValues.append(values) # type: ignore[arg-type] + timeUnit: str = self.m_propertiesUnit["time"].unitLabel + timeName: str = "Time__" + timeUnit + dtName: str = "dt__" + timeUnit + colNames.append(timeName) + colNames.append(dtName) + colValues.append(self.m_timesteps) # type: ignore[arg-type] + colValues.append(self.m_dts) # type: ignore[arg-type] + data = {colNames[i]: colValues[i] for i in range(len(colNames))} + dataframeSolversIterations: pd.DataFrame = pd.DataFrame(data) + return dataframeSolversIterations diff --git a/geos-posp/src/geos_posp/readers/GeosLogReaderFlow.py b/geos-posp/src/geos_posp/readers/GeosLogReaderFlow.py new file mode 100644 index 00000000..506cf736 --- /dev/null +++ b/geos-posp/src/geos_posp/readers/GeosLogReaderFlow.py @@ -0,0 +1,224 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +from io import TextIOBase +from typing import Union + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +import geos_posp.processing.geosLogReaderFunctions as fcts +from geos_posp.utils.enumUnits import Unit + + +class GeosLogReaderFlow: + def __init__( + self: Self, + filepath: str, + propertiesUnit: dict[str, Unit], + phaseNames: Union[list[str], None] = None, + ) -> None: + """A reader that reads .txt and .out files containing Geos logs. + + To do that, we use specific tags in the current version of this code. + Supposed tags are: + + * for region names: "Adding Object CellElementRegion" Supposed + line:"Adding Object CellElementRegion named Reservoir from + ObjectManager::Catalog". + * for phase names: "phaseModel" Supposed line: " TableFunction: + fluid_phaseModel1_PhillipsBrineDensity_table". + * for timesteps: "Time:" Supposed line: "Time: 0s, dt:100s, Cycle: 0". + * for CFL properties: "CFL". Supposed line: "compflowStatistics: Max + phase CFL number: 0.00696878" + + Another important tag in the log will be the name + of the flow statistics model used to output 2D data + in the Geos Log. This one will be found automatically. + The flow statistics model that can output flow data are: + + * "SinglePhaseStatistics". + * "CompositionalMultiphaseStatistics". + + Args: + filepath (str): path to Geos log file + propertiesUnit (dict[str, Unit]): unit preferences + phaseNames (list[str], optional): Name of the phases. + + Defaults to []. + """ + self.m_propertiesUnit = propertiesUnit + self.m_regionNames: list[str] = [] + numberPhases: int = fcts.findNumberPhasesSimulation(filepath) + + if phaseNames is None: + phaseNames = [] + self.m_phaseNames: list[str] = fcts.phaseNamesBuilder(numberPhases, phaseNames) + self.m_computeStatisticsName: str = "" + self.m_regionsPropertiesValues: dict[str, list[float]] = {} + self.m_timesteps: list[float] = [] + + toFindInLog: list[str] = ["Adding Object CellElementRegion", "Time: 0"] + if not fcts.elementsAreInLog(filepath, toFindInLog): + print( + "Invalid Geos log file. Please check that your log" + + " did not crash and contains statistics on flow properties." + ) + else: + self.readAll(filepath) + + def readRegionNames(self: Self, file: TextIOBase) -> int: + """Initialize the m_regionNames attribute by reading log file. + + Args: + file (TextIOBase): Geos Log file + + Returns: + int: The id of the last line read that contained the tag + "Adding Object CellElementRegion" + """ + regionsName: list[str] = [] + line: str = file.readline() + id_line: int = 1 + while "Adding Object CellElementRegion" not in line: + line = file.readline() + id_line += 1 + while "Adding Object CellElementRegion" in line: + regionName: str = fcts.extractRegion(line) + regionsName.append(regionName) + line = file.readline() + id_line += 1 + self.m_regionNames = regionsName + return id_line + + def readComputeStatisticsName( + self: Self, file: TextIOBase, id_line: int, total_lines: int + ) -> tuple[int, str]: + """Read flow statistics from the Geos log file. + + Args: + file (TextIOBase): Geos Log file + id_line (int): The id of the last line read in readPhaseNames. + total_lines (int): total number of lines in the file. + + Returns: + tuple[int, str]: Tuple containingt the id of the last line read and + the line. + """ + computeStatisticsName: str = "" + line: str = file.readline() + id_line += 1 + while not line.startswith("Time: 0"): + line = file.readline() + id_line += 1 + keepReading: bool = True + while keepReading: + line = file.readline() + id_line += 1 + if id_line > total_lines: + raise ValueError("No statistics name found in the log") + for regionName in self.m_regionNames: + if regionName in line: + computeStatisticsName = fcts.extractStatsName(line) + keepReading = False + break + self.m_computeStatisticsName = computeStatisticsName + return (id_line, line) + + def readPropertiesValues( + self: Self, file: TextIOBase, id_line: int, total_lines: int, lineTagStats: str + ) -> None: + """Read property values from Geos log file. + + Initialize the m_regionsPropertiesValues and m_timesteps attributes + by reading the Geos log. If a timestep contains the tag + m_computeStatisticsName, the current timestep is added to m_timesteps + and we recover the property values in m_regionsPropertiesValues. + + Args: + file (TextIOBase): Geos Log file + id_line (int): The id of the last line read in readPhaseNames. + total_lines (int): The number of lines in the file. + lineTagStats (str): The first line containing the tag of + the flow statistics model. + """ + regionPropertiesValues: dict[str, list[float]] = {} + newTimestep: float = 0.0 + timesteps: list[float] = [newTimestep] + line: str = lineTagStats + while id_line <= total_lines: + if line.startswith("Time:"): + newTimestep, dt = fcts.extractTimeAndDt(line) + newTimestep = fcts.convertValues( + ["Time"], [newTimestep], self.m_propertiesUnit + )[0] + if self.m_computeStatisticsName in line and "CFL" not in line: + if newTimestep not in timesteps and newTimestep > max( + timesteps, default=0.0 + ): + timesteps.append(newTimestep) + for key in regionPropertiesValues: + regionPropertiesValues[key].append(0.0) + propsName: list[str] = fcts.extractPropertiesFlow( + line, self.m_phaseNames + ) + propsNameId: list[str] = fcts.identifyProperties(propsName) + for propNameId in propsNameId: + if propNameId not in regionPropertiesValues: + regionPropertiesValues[propNameId] = [0.0] + propsValue: list[float] = fcts.extractValuesFlow(line) + valuesConverted: list[float] = fcts.convertValues( + propsName, propsValue, self.m_propertiesUnit + ) + for i, name in enumerate(propsNameId): + regionPropertiesValues[name][-1] = valuesConverted[i] + line = file.readline() + id_line += 1 + self.m_regionsPropertiesValues = regionPropertiesValues + self.m_timesteps = timesteps + + def readAll(self: Self, filepath: str) -> None: + """Initialize all the attributes of the class by reading a Geos log file. + + Args: + filepath (str): Geos log filepath. + """ + with open(filepath) as geosFile: + total_lines: int = fcts.countNumberLines(filepath) + id_line: int = self.readRegionNames(geosFile) + id_line, lineTag = self.readComputeStatisticsName( + geosFile, id_line, total_lines + ) + self.readPropertiesValues(geosFile, id_line, total_lines, lineTag) + + def createDataframe(self: Self) -> pd.DataFrame: + """Create and fill and return dataframeFlow. + + Returns: + pd.DataFrame: dataframe with values from Geos log. + """ + try: + colNames: list[str] = [] + colValues: list[float] = [] + for propName, values in self.m_regionsPropertiesValues.items(): + unitObj: Unit = self.m_propertiesUnit["nounit"] + for propertyType in self.m_propertiesUnit: + if propertyType in propName.lower(): + unitObj = self.m_propertiesUnit[propertyType] + break + if unitObj.unitLabel == "": + raise ValueError( + "No unit was found for this property name <<" + propName + ">>." + ) + columnName: str = propName + "__" + unitObj.unitLabel + colNames.append(columnName) + colValues.append(values) # type: ignore[arg-type] + timeUnit: str = self.m_propertiesUnit["time"].unitLabel + timeName: str = "Time__" + timeUnit + colNames.append(timeName) + colValues.append(self.m_timesteps) # type: ignore[arg-type] + data = {colNames[i]: colValues[i] for i in range(len(colNames))} + dataframeFlow: pd.DataFrame = pd.DataFrame(data) + return dataframeFlow + except ValueError as err: + print(err.args[0]) diff --git a/geos-posp/src/geos_posp/readers/GeosLogReaderWells.py b/geos-posp/src/geos_posp/readers/GeosLogReaderWells.py new file mode 100644 index 00000000..af420e30 --- /dev/null +++ b/geos-posp/src/geos_posp/readers/GeosLogReaderWells.py @@ -0,0 +1,293 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +from io import TextIOBase +from typing import Union + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +import geos_posp.processing.geosLogReaderFunctions as fcts +from geos_posp.utils.enumUnits import Unit + + +class GeosLogReaderWells: + def __init__( + self: Self, + filepath: str, + propertiesUnit: dict[str, Unit], + phaseNames: Union[list[str], None] = None, + numberWellsForMean: int = 1, + ) -> None: + """Read for Wells from Geos log file. + + To do that, we use specific tags in the current version of this code. + Supposed tags are : + + * for well names : "Adding object WellElementRegion" + and "_ConstantBHP_table" Supposed lines: + "Adding Object WellElementRegion named + wellRegion1 from ObjectManager::Catalog". + " TableFunction: wellControls1_ConstantBHP_table". + * for phase names: "phaseModel" + Supposed line: " TableFunction: + fluid_phaseModel1_PhillipsBrineDensity_table". + * for timesteps: "Time:" + Supposed line : "Time: 0s, dt:100s, Cycle: 0" + When it comes to well properties, special tags are used : + " BHP " ; " total rate" ; " total surface volumetric rate" ; + "phase surface volumetric rate" ; "well is shut" ; + "density of phase" ; "total fluid density". + + Args: + filepath (str): path of Geos log file + propertiesUnit (dict[str, Unit]): unit preferences + phaseNames (list[str] | None, optional): Name of the phases. + + Defaults to None. + numberWellsForMean (int, optional): Number of wells. Defaults to 1. + """ + self.m_propertiesUnit: dict[str, Unit] = propertiesUnit + self.m_numberWellsForMean: int = numberWellsForMean + self.m_wellNames: list[str] = [] + numberPhases: int = fcts.findNumberPhasesSimulation(filepath) + + if phaseNames is None: + phaseNames = [] + self.m_phaseNames: list[str] = fcts.phaseNamesBuilder(numberPhases, phaseNames) + self.m_wellsPropertiesValues: dict[str, list[float]] = {} + self.m_timesteps: list[float] = [] + + toFindInLog1: list[str] = [ + "_ConstantBHP_table", + "Time: 0", + " TableFunction: ", + ] + toFindInLog2: list[str] = [ + "_ConstantPhaseRate_table", + "Time: 0", + " TableFunction: ", + ] + foundInLog1: bool = fcts.elementsAreInLog(filepath, toFindInLog1) + foundInLog2: bool = fcts.elementsAreInLog(filepath, toFindInLog2) + if not foundInLog1 or not foundInLog2: + print( + "Invalid Geos log file. Please check that your log" + + " did not crash and contains wells." + ) + else: + self.readAll(filepath) + self.calculateMeanValues() + + def readWellNames(self: Self, file: TextIOBase) -> int: + """Read well names from Geos log file. + + Args: + file (TextIOBase): Geos Log file + id_line (int): The id of the last line read in readPhaseNames. + + Returns: + int: The id of the last line read that contains the tag + "Adding Object WellElementRegion". + """ + wellsName: list[str] = [] + line: str = file.readline() + id_line: int = 1 + intoWellNames: bool = False + while not intoWellNames: + line = file.readline() + id_line += 1 + if "_ConstantBHP_table" in line or "_ConstantPhaseRate_table" in line: + intoWellNames = True + intoTableFunctions: bool = True + while intoTableFunctions: + if "_ConstantBHP_table" in line or "_ConstantPhaseRate_table" in line: + wellName: str = fcts.extractWell(line) + if wellName not in wellsName: + wellsName.append(wellName) + line = file.readline() + id_line += 1 + if " TableFunction: " not in line: + intoTableFunctions = False + self.m_wellNames = wellsName + return id_line + + def initWellPropertiesValues(self: Self) -> None: + """Initialize the m_wellPropertiesValues.""" + props: dict[str, list[float]] = {} + for name in self.m_wellNames: + wName: str = fcts.formatPropertyName(name) + bhp: str = wName + "__BHP" + totalMassRate: str = wName + "__TotalMassRate" + totalSVR: str = wName + "__TotalSurfaceVolumetricRate" + propsNoId: list[str] = [bhp, totalMassRate, totalSVR] + if len(self.m_phaseNames) > 1: + for phase in self.m_phaseNames: + pName: str = fcts.formatPropertyName(phase) + phaseSVR: str = wName + "__SurfaceVolumetricRate" + pName + propsNoId.append(phaseSVR) + propsWithId = fcts.identifyProperties(propsNoId) + for propName in propsWithId: + props[propName] = [0.0] + self.m_wellsPropertiesValues = props + + def readPropertiesValues( + self: Self, file: TextIOBase, id_line: int, total_lines: int + ) -> None: + """Read property values from Geos log file. + + Initialize the m_regionsPropertiesValues and m_timesteps attributes + by reading the Geos log. If a timestep contains the tag + m_computeStatisticsName, the current timestep is added to m_timesteps + and we recover the property values in m_regionsPropertiesValues. + + Args: + file (TextIOBase): Geos Log file + id_line (int): The id of the last line read in readPhaseNames. + total_lines (int): The number of lines in the file. + """ + line: str = file.readline() + id_line += 1 + while not line.startswith("Time: 0"): + line = file.readline() + id_line += 1 + wellsPropertiesValues: dict[str, list[float]] = self.m_wellsPropertiesValues + currentWellName: str = self.m_wellNames[0] + currentPhaseName: str = self.m_phaseNames[0] + newTimestep: float = 0.0 + timesteps: list[float] = [newTimestep] + while id_line <= total_lines: + wellTags = fcts.extractWellTags(line) + if line.startswith("Time:"): + newTimestep, dt = fcts.extractTimeAndDt(line) + newTimestep = fcts.convertValues( + ["Time"], [newTimestep], self.m_propertiesUnit + )[0] + # If at least one well tag is found, this is a well line + if len(wellTags) > 0: + if newTimestep not in timesteps and newTimestep > max( + timesteps, default=0.0 + ): + timesteps.append(newTimestep) + for key in wellsPropertiesValues: + wellsPropertiesValues[key].append(0.0) + newWellName: str = fcts.identifyCurrentWell(line, currentWellName) + if newWellName != currentWellName: + if newWellName in self.m_wellNames: + currentWellName = newWellName + else: + print( + f"Invalid well name <<{newWellName}>> found" + + f" at timestep <<{str(newTimestep)}>>" + + f" in line :\n<<{line}>>.\nAnother correct well" + + f" name <<{currentWellName}>> was used to" + + " correct this.\nExpected well names are :" + + f" {str(self.m_wellNames)}.\n" + ) + if ("phase" in line.lower()) and ("phase surface" not in line.lower()): + newPhaseId: int = fcts.extractPhaseId(line) + if self.m_phaseNames[newPhaseId] != currentWellName: + currentPhaseName = self.m_phaseNames[newPhaseId] + propsName: list[str] = fcts.extractPropertiesWell( + line, currentWellName, currentPhaseName + ) + for name in propsName: + if "density" in name.lower(): + propsName.pop(propsName.index(name)) + if len(propsName) > 0 and "IsShut" not in propsName[0]: + propsNameId: list[str] = fcts.identifyProperties(propsName) + propsValue: list[float] = fcts.extractValuesWell( + line, len(propsName) + ) + valuesConverted: list[float] = fcts.convertValues( + propsName, propsValue, self.m_propertiesUnit + ) + for i, name in enumerate(propsNameId): + wellsPropertiesValues[name][-1] = valuesConverted[i] + + line = file.readline() + id_line += 1 + self.m_wellsPropertiesValues = wellsPropertiesValues + self.m_timesteps = timesteps + + def readAll(self: Self, filepath: str) -> None: + """Initialize all the attributes of the class by reading a Geos log file. + + Args: + filepath (str): Geos log filepath. + singlephase (bool): True if its a singlephase simulation, + False if multiphase. + """ + with open(filepath) as geosFile: + total_lines: int = fcts.countNumberLines(filepath) + id_line = self.readWellNames(geosFile) + self.initWellPropertiesValues() + self.readPropertiesValues(geosFile, id_line, total_lines) + + def calculateMeanValues(self: Self) -> None: + """Calculate mean values of all wells.""" + nbr: int = self.m_numberWellsForMean + wNames: list[str] = self.m_wellNames + pNames: list[str] = self.m_phaseNames + wpv: dict[str, list[float]] = self.m_wellsPropertiesValues + cNames: list[str] = list(wpv.keys()) + bhpNames: list[str] = [n for n in cNames if "bhp" in n.lower()] + totalMassRateNames: list[str] = [ + n for n in cNames if "totalmassrate" in n.lower() + ] + totalSVRNames: list[str] = [ + n for n in cNames if "totalsurfacevolumetricrate" in n.lower() + ] + differentMeanColumns: dict[str, list[str]] = { + "MeanBHP": bhpNames, + "MeanTotalMassRate": totalMassRateNames, + "MeanTotalVolumetricRate": totalSVRNames, + } + for pName in pNames: + pName = fcts.formatPropertyName(pName) + meanName: str = "MeanSurfaceVolumetricRate" + pName + differentMeanColumns[meanName] = [] + for wName in wNames: + wName = fcts.formatPropertyName(wName) + n: str = wName + "__SurfaceVolumetricRate" + pName + n = fcts.identifyProperties([n])[0] + if n in cNames: + differentMeanColumns[meanName].append(n) + for meanName, columns in differentMeanColumns.items(): + if len(columns) > 0: + values: list[list[float]] = [wpv[c] for c in columns] + meanValues: list[float] = [sum(item) / nbr for item in zip(*values)] + meanNameWithId: str = fcts.identifyProperties([meanName])[0] + self.m_wellsPropertiesValues[meanNameWithId] = meanValues + + def createDataframe(self: Self) -> pd.DataFrame: + """Create and fill and return dataframeWells. + + Return: + pd.DataFrame: dataframe with log values. + """ + colNames: list[str] = [] + colValues: list[float] = [] + try: + for propName, values in self.m_wellsPropertiesValues.items(): + unitObj: Unit = self.m_propertiesUnit["nounit"] + for propertyType in self.m_propertiesUnit: + if propertyType.lower() in propName.lower(): + unitObj = self.m_propertiesUnit[propertyType] + break + if unitObj.unitLabel == "": + raise ValueError( + "No unit was found for this property name <<" + propName + ">>." + ) + columnName: str = propName + "__" + unitObj.unitLabel + colNames.append(columnName) + colValues.append(values) # type: ignore[arg-type] + except ValueError as err: + print(err.args[0]) + timeUnit: str = self.m_propertiesUnit["time"].unitLabel + timeName: str = "Time__" + timeUnit + colNames.append(timeName) + colValues.append(self.m_timesteps) # type: ignore[arg-type] + data = {colNames[i]: colValues[i] for i in range(len(colNames))} + dataframeWells: pd.DataFrame = pd.DataFrame(data) + return dataframeWells diff --git a/geos-posp/src/geos_posp/readers/__init__.py b/geos-posp/src/geos_posp/readers/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/utils/GeosOutputsConstants.py b/geos-posp/src/geos_posp/utils/GeosOutputsConstants.py new file mode 100644 index 00000000..374d3fd7 --- /dev/null +++ b/geos-posp/src/geos_posp/utils/GeosOutputsConstants.py @@ -0,0 +1,298 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +from enum import Enum + +from typing_extensions import Self + +__doc__ = """ +GeosOutputsConstants module defines usefull constant names such as attribute +names, domain names, phase types, and the lists of attribute names to process. +""" + +#: Phase separator in Geos output log file. +PHASE_SEP: str = "_" +FAILURE_ENVELOPE: str = "FailureEnvelope" + + +class AttributeEnum(Enum): + def __init__( + self: Self, attributeName: str, nbComponent: int, onPoints: bool + ) -> None: + """Define the enumeration to store attrbute properties. + + Args: + attributeName (str): name of the attribute + nbComponent (int): number of component: 1 is scalar attribute, >1 is + vectorial attribute + onPoints (bool): location of the attribute: on Points (True) or on Cells + (False) + """ + self.attributeName: str = attributeName + self.nbComponent: int = nbComponent + self.isOnPoints: bool = onPoints + + def __repr__(self: Self) -> str: + """Get the string of AttributeEnum. + + Returns: + str: string of AttributeEnum. + """ + return f"<{self.__class__.__name__}.{self.attributeName}>.{self.nbComponent}>" + + +################################################################################ +# Searched keywords in geos log # +################################################################################ +class GeosLogOutputsEnum(Enum): + """Define the keywords in Geos log.""" + + # flow keywords + PHASE = "phase" + + # well keywords + + # aquifer keywords + + # convergence keywords + + +################################################################################ +# Attribute names in the output mesh # +################################################################################ + + +# list of node names from Geos +class GeosDomainNameEnum(Enum): + """Name of the nodes in the MultiBlock data tree.""" + + VOLUME_DOMAIN_NAME = "CellElementRegion" + FAULT_DOMAIN_NAME = "SurfaceElementRegion" + WELL_DOMAIN_NAME = "WellElementRegion" + + +# Attributes are defined according to a tuple (str, int, bool) that contains the +# name of the attribute, the number of components for vectorial attributes and +# a boolean that evaluates to True if the attribute is stored on Points, and False +# if it is stored on Cells + + +class GeosMeshSuffixEnum(Enum): + """Define the suffix of attributes in Geos output mesh.""" + + # rock attributes suffix + DENSITY_SUFFIX = "_density" + STRESS_SUFFIX = "_stress" + STRAIN_SUFFIX = "strain" + PERMEABILITY_SUFFIX = "_permeability" + POROSITY_SUFFIX = "_porosity" + POROSITY_REF_SUFFIX = "_referencePorosity" + BULK_MODULUS_SUFFIX = "_bulkModulus" + SHEAR_MODULUS_SUFFIX = "_shearModulus" + GRAIN_BULK_MODULUS_SUFFIX = "_grainBulkModulus" + BIOT_COEFFICIENT_SUFFIX = "_biotCoefficient" + + # fluid attributes suffix + PHASE_DENSITY_SUFFIX = "_phaseDensity" + PHASE_MASS_DENSITY_SUFFIX = "_phaseMassDensity" + PHASE_VISCOSITY_SUFFIX = "_phaseViscosity" + PHASE_FRACTION_SUFFIX = "_phaseFraction" + + # surface attribute transfer suffix + SURFACE_PLUS_SUFFIX = "_Plus" + SURFACE_MINUS_SUFFIX = "_Minus" + + +class GeosMeshOutputsEnum(AttributeEnum): + """Attribute names that come from Geos. + + Define the names of Geos outputs, the number of components + for vectorial attributes, and the location (Point or Cell) in the mesh + """ + + # IDs + POINTS_ID = ("Point ID", 1, True) + CELL_ID = ("Cell ID", 1, False) + VTK_ORIGINAL_CELL_ID = ("vtkOriginalCellIds", 1, False) + + # geometry attributes + POINT = ("Points", 3, True) + ELEMENT_CENTER = ("elementCenter", 1, False) + + # flow attributes + WATER_DENSITY = ("water_density", 1, False) + PRESSURE = ("pressure", 1, False) + DELTA_PRESSURE = ("deltaPressure", 1, False) + MASS = ("mass", 1, False) + + # geomechanic attributes + ROCK_DENSITY = ("density", 1, False) + PERMEABILITY = ("permeability", 1, False) + POROSITY = ("porosity", 1, False) + POROSITY_INI = ("porosityInitial", 1, False) + + BULK_MODULUS = ("bulkModulus", 1, False) + GRAIN_BULK_MODULUS = ("bulkModulusGrains", 1, False) + SHEAR_MODULUS = ("shearModulus", 1, False) + STRESS_EFFECTIVE = ("stressEffective", 6, False) + TOTAL_DISPLACEMENT = ("totalDisplacement", 4, True) + + TRACTION = ("traction", 3, False) + DISPLACEMENT_JUMP = ("displacementJump", 3, False) + + +################################################################################ +# Post-processing attribute names # +################################################################################ + + +class PostProcessingOutputsEnum(AttributeEnum): + """Compute attributes enumeration. + + Define the names of post-processing outputs, the number of components + for vectorial attributes, and the location (Point or Cell) in the mesh + """ + + # general outputs + BLOCK_INDEX = ("blockIndex", 1, False) + ADJACENT_CELL_SIDE = ("SurfaceAdjacentCells", 1, False) + + # basic geomechanical outputs + BULK_MODULUS_INITIAL = ("bulkModulusInitial", 1, False) + SHEAR_MODULUS_INITIAL = ("shearModulusInitial", 1, False) + YOUNG_MODULUS = ("youngModulus", 1, False) + YOUNG_MODULUS_INITIAL = ("youngModulusInitial", 1, False) + POISSON_RATIO = ("poissonRatio", 1, False) + POISSON_RATIO_INITIAL = ("poissonRatioInitial", 1, False) + OEDOMETRIC_MODULUS = ("oedometricModulus", 1, False) + BIOT_COEFFICIENT = ("biotCoefficient", 1, False) + BIOT_COEFFICIENT_INITIAL = ("biotCoefficientInitial", 1, False) + COMPRESSIBILITY = ("compressibilityCoefficient", 1, False) + COMPRESSIBILITY_REAL = ("compressibilityCoefficient_real", 1, False) + COMPRESSIBILITY_OED = ("compressibilityCoefficient_oed", 1, False) + SPECIFIC_GRAVITY = ("specificGravity", 1, False) + LITHOSTATIC_STRESS = ("stressLithostatic", 1, False) + STRESS_EFFECTIVE_INITIAL = ("stressEffectiveInitial", 6, False) + STRESS_EFFECTIVE_RATIO_REAL = ("stressEffectiveRatio_real", 6, False) + STRESS_EFFECTIVE_RATIO_OED = ("stressEffectiveRatio_oed", 6, False) + STRESS_TOTAL = ("stressTotal", 6, False) + STRESS_TOTAL_INITIAL = ("stressTotalInitial", 6, False) + STRESS_TOTAL_RATIO_REAL = ("stressTotalRatio_real", 6, False) + STRESS_TOTAL_DELTA = ("deltaStressTotal", 6, False) + STRAIN_ELASTIC = ("strainElastic", 6, False) + RSP_OED = ("rsp_oed", 1, False) + RSP_REAL = ("rsp_real", 6, False) + + # advanced geomechanical outputs + CRITICAL_TOTAL_STRESS_RATIO = ("totalStressRatioCritical_real", 1, False) + TOTAL_STRESS_RATIO_THRESHOLD = ("totalStressRatioThreshold_real", 1, False) + CRITICAL_PORE_PRESSURE = ("porePressureCritical_real", 1, False) + CRITICAL_PORE_PRESSURE_THRESHOLD = ("porePressureThreshold_real", 1, False) + + # surface outputs + SCU = ("SCU", 1, False) + + +class PhaseTypeEnum(Enum): + def __init__(self: Self, phaseType: str, attributes: tuple[str, ...]) -> None: + """Define the main phases and associated property suffix. + + Args: + phaseType (str): name of the type of phase + + attributes (tuple[str,...]): list of attributes + """ + self.type: str = phaseType + self.attributes: tuple[str, ...] = attributes + + ROCK = ( + "Rock", + ( + GeosMeshSuffixEnum.DENSITY_SUFFIX.value, + GeosMeshSuffixEnum.STRESS_SUFFIX.value, + GeosMeshSuffixEnum.BULK_MODULUS_SUFFIX.value, + GeosMeshSuffixEnum.SHEAR_MODULUS_SUFFIX.value, + GeosMeshSuffixEnum.POROSITY_SUFFIX.value, + GeosMeshSuffixEnum.POROSITY_REF_SUFFIX.value, + GeosMeshSuffixEnum.PERMEABILITY_SUFFIX.value, + ), + ) + FLUID = ( + "Fluid", + ( + GeosMeshSuffixEnum.PHASE_DENSITY_SUFFIX.value, + GeosMeshSuffixEnum.PHASE_VISCOSITY_SUFFIX.value, + GeosMeshSuffixEnum.PHASE_FRACTION_SUFFIX.value, + GeosMeshSuffixEnum.PHASE_MASS_DENSITY_SUFFIX.value, + ), + ) + UNKNOWN = ("Other", ()) + + +class FluidPrefixEnum(Enum): + """Define usual names used for the fluid phase.""" + + WATER = "water" + FLUID = "fluid" + GAS = "gas" + + +class OutputObjectEnum(Enum): + """Kind of objects present in GEOS pvd output.""" + + VOLUME = "Volume" + FAULTS = "Faults" + WELLS = "Wells" + + +class ComponentNameEnum(Enum): + NONE = ("",) + XYZ = ("XX", "YY", "ZZ", "YZ", "XZ", "XY") + NORMAL_TANGENTS = ("normal", "tangent1", "tangent2", "T1T2", "NT2", "NT1") + + +def getRockSuffixRenaming() -> dict[str, str]: + """Get the list of attributes to rename according to suffix. + + Returns: + dict[str,str]: dictionary where suffix are keys and new names are values + """ + return { + GeosMeshSuffixEnum.DENSITY_SUFFIX.value: GeosMeshOutputsEnum.ROCK_DENSITY.attributeName, + GeosMeshSuffixEnum.STRESS_SUFFIX.value: GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName, + GeosMeshSuffixEnum.PERMEABILITY_SUFFIX.value: GeosMeshOutputsEnum.PERMEABILITY.attributeName, + GeosMeshSuffixEnum.POROSITY_SUFFIX.value: GeosMeshOutputsEnum.POROSITY.attributeName, + GeosMeshSuffixEnum.POROSITY_REF_SUFFIX.value: GeosMeshOutputsEnum.POROSITY_INI.attributeName, + GeosMeshSuffixEnum.BULK_MODULUS_SUFFIX.value: GeosMeshOutputsEnum.BULK_MODULUS.attributeName, + GeosMeshSuffixEnum.SHEAR_MODULUS_SUFFIX.value: GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName, + GeosMeshSuffixEnum.GRAIN_BULK_MODULUS_SUFFIX.value: GeosMeshOutputsEnum.GRAIN_BULK_MODULUS.attributeName, + GeosMeshSuffixEnum.BIOT_COEFFICIENT_SUFFIX.value: PostProcessingOutputsEnum.BIOT_COEFFICIENT.attributeName, + GeosMeshSuffixEnum.STRAIN_SUFFIX.value: PostProcessingOutputsEnum.STRAIN_ELASTIC.attributeName, + } + + +def getAttributeToTransferFromInitialTime() -> dict[str, str]: + """Get the list of attributes to copy from initial time step. + + Returns: + dict[str,str]: dictionary where attribute names are keys and copied + names are values + """ + return { + GeosMeshOutputsEnum.STRESS_EFFECTIVE.attributeName: PostProcessingOutputsEnum.STRESS_EFFECTIVE_INITIAL.attributeName, + GeosMeshOutputsEnum.SHEAR_MODULUS.attributeName: PostProcessingOutputsEnum.SHEAR_MODULUS_INITIAL.attributeName, + GeosMeshOutputsEnum.BULK_MODULUS.attributeName: PostProcessingOutputsEnum.BULK_MODULUS_INITIAL.attributeName, + PostProcessingOutputsEnum.YOUNG_MODULUS.attributeName: PostProcessingOutputsEnum.YOUNG_MODULUS_INITIAL.attributeName, + PostProcessingOutputsEnum.POISSON_RATIO.attributeName: PostProcessingOutputsEnum.POISSON_RATIO_INITIAL.attributeName, + } + + +def getAttributeToConvertFromLocalToXYZ() -> set[str]: + """Get the list of attribute names to convert from local to xyz basis. + + Returns: + list[str]: list of attributes to convert + """ + return { + GeosMeshOutputsEnum.DISPLACEMENT_JUMP.attributeName, + } diff --git a/geos-posp/src/geos_posp/utils/Logger.py b/geos-posp/src/geos_posp/utils/Logger.py new file mode 100644 index 00000000..c7ef2d89 --- /dev/null +++ b/geos-posp/src/geos_posp/utils/Logger.py @@ -0,0 +1,115 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +import logging +from typing import Union + +from typing_extensions import Self + +__doc__ = """ +Logger module manages logging tools. + +Code was modified from +""" + +# types redefinition to import logging.* from this module +Logger = logging.Logger #: logger type + +DEBUG: int = logging.DEBUG +INFO: int = logging.INFO +WARNING: int = logging.WARNING +ERROR: int = logging.ERROR +CRITICAL: int = logging.CRITICAL + + +class CustomLoggerFormatter(logging.Formatter): + """Custom formatter for the logger. + + .. WARNING:: Colors do not work in the ouput message window of Paraview. + + To use it: + + .. code-block:: python + + logger = logging.getLogger("Logger name") + ch = logging.StreamHandler() + ch.setFormatter(CustomLoggerFormatter()) + logger.addHandler(ch) + """ + + # define color codes + grey: str = "\x1b[38;20m" + yellow: str = "\x1b[33;20m" + red: str = "\x1b[31;20m" + bold_red: str = "\x1b[31;1m" + reset: str = "\x1b[0m" + # define prefix of log messages + format1: str = "%(asctime)s - %(name)s - %(levelname)s - %(message)s" + format2: str = ( + "%(asctime)s - %(name)s - %(levelname)s - %(message)s (%(filename)s:%(lineno)d)" + ) + + #: format for each logger output type + FORMATS: dict[int, str] = { + DEBUG: grey + format2 + reset, + INFO: grey + format1 + reset, + WARNING: yellow + format1 + reset, + ERROR: red + format1 + reset, + CRITICAL: bold_red + format2 + reset, + } + + #: same without colors + FORMATS_PV: dict[int, str] = { + DEBUG: format2, + INFO: format1, + WARNING: format1, + ERROR: format1, + CRITICAL: format2, + } + + def format(self: Self, record: logging.LogRecord) -> str: + """Return the format according to input record. + + Args: + record (logging.LogRecord): record + + Returns: + str: format as a string + """ + log_fmt: Union[str, None] = self.FORMATS_PV.get(record.levelno) + formatter = logging.Formatter(log_fmt) + return formatter.format(record) + + +def getLogger(title: str) -> Logger: + """Return the Logger with pre-defined configuration. + + Example: + + .. code-block:: python + + # module import + import Logger + + # logger instanciation + logger :Logger.Logger = Logger.getLogger("My application") + + # logger use + logger.debug("debug message") + logger.info("info message") + logger.warning("warning message") + logger.error("error message") + logger.critical("critical message") + + Args: + title (str): Name of the logger. + + Returns: + Logger: logger + """ + logger: Logger = logging.getLogger(title) + logger.setLevel(logging.INFO) + ch = logging.StreamHandler() + ch.setFormatter(CustomLoggerFormatter()) + logger.addHandler(ch) + return logger diff --git a/geos-posp/src/geos_posp/utils/PhysicalConstants.py b/geos-posp/src/geos_posp/utils/PhysicalConstants.py new file mode 100644 index 00000000..8292a802 --- /dev/null +++ b/geos-posp/src/geos_posp/utils/PhysicalConstants.py @@ -0,0 +1,24 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay + +__doc__ = """Define default values of usefull physical constants.""" + +import numpy as np + +EPSILON: float = 1e-6 #: epsilon + +GRAVITY: float = 9.81 #: gravity (m/s) + +WATER_DENSITY: float = 1000.0 #: water density (kg/m³) +WATER_DYNAMIC_VISCOSITY: float = 1e-3 #: water dynamic viscosity (kg.m^-1/s^-1 = Pa.s) +WATER_KINEMATIC_VISCOSITY: float = 1e-6 #: water kinematic viscosity (m²/s) + +#: default grain bulk modulus is that of Quartz (Pa) +DEFAULT_GRAIN_BULK_MODULUS: float = 38e9 +#: default rock cohesion - fractured case - (Pa) +DEFAULT_ROCK_COHESION: float = 0.0 +#: default friction angle (rad) +DEFAULT_FRICTION_ANGLE_RAD: float = 10.0 / 180.0 * np.pi +#: default friction angle (deg) +DEFAULT_FRICTION_ANGLE_DEG: float = DEFAULT_FRICTION_ANGLE_RAD * 180.0 / np.pi diff --git a/geos-posp/src/geos_posp/utils/UnitRepository.py b/geos-posp/src/geos_posp/utils/UnitRepository.py new file mode 100644 index 00000000..5984bff9 --- /dev/null +++ b/geos-posp/src/geos_posp/utils/UnitRepository.py @@ -0,0 +1,57 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +from enum import Enum +from typing import Union + +from typing_extensions import Self + +from geos_posp.utils.enumUnits import Unit, getPropertyUnitEnum, getSIUnits + + +class UnitRepository: + def __init__( + self: Self, userPropertiesUnitChoice: Union[dict[str, int], None] = None + ) -> None: + """Unit repository. + + * Input example : { "pressure": 4, "bhp": 4,"stress": 3, "length": 2, ...} + * Output example : { "pressure": Pressure.BAR.value, "bhp": Pressure.BAR.value, + "stress": Pressure.MPA.value, "length": Lenght.FEET.value, + ... + } + + These Pressure.BAR.value corresponds to Unit objects that have a + conversion multiplier and a conversion adder, and also a unit label. + + Args: + userPropertiesUnitChoice (dict[str, int], Optional): dictionary of + unit user choices. + + Defaults {}. + """ + self.m_userPropsUnitChoice: dict[str, int] = {} + if userPropertiesUnitChoice is not None: + self.m_userPropsUnitChoice = userPropertiesUnitChoice + + self.m_propertiesUnit: dict[str, Unit] = getSIUnits() + if self.m_userPropsUnitChoice != {}: + self.initPropertiesUnit() + + def initPropertiesUnit(self: Self) -> None: + """Initialize the attribute m_propertiesUnit.""" + propertiesUnit: dict[str, Unit] = getSIUnits() + for propertyName, userChoice in self.m_userPropsUnitChoice.items(): + unitEnum: Enum = getPropertyUnitEnum(propertyName) + unitObj: Unit = list(unitEnum)[userChoice].value # type: ignore[call-overload] + propertiesUnit[propertyName] = unitObj + self.m_propertiesUnit = propertiesUnit + + def getPropertiesUnit(self: Self) -> dict[str, Unit]: + """Access the m_propertiesUnit attribute. + + Returns: + dict[str, Unit]: dictionary of unit as values for each property as + keys. + """ + return self.m_propertiesUnit diff --git a/geos-posp/src/geos_posp/utils/__init__.py b/geos-posp/src/geos_posp/utils/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/utils/enumUnits.py b/geos-posp/src/geos_posp/utils/enumUnits.py new file mode 100644 index 00000000..07130cd1 --- /dev/null +++ b/geos-posp/src/geos_posp/utils/enumUnits.py @@ -0,0 +1,189 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +# Units conversion factors chosen in this file are from +# https://www.petrobasics.com/unit-convert +from enum import Enum +from typing import cast + +from typing_extensions import Self + + +class Unit: + def __init__( + self: Self, conversionMultiplier: float, conversionAdder: float, unitLabel: str + ) -> None: + """Unit enumeration. + + Args: + conversionMultiplier (float): conversion multiplier + conversionAdder (float): conversion adder + unitLabel (str): symbol of the unit. + """ + self.conversionMultiplier: float = conversionMultiplier + self.conversionAdder: float = conversionAdder + self.unitLabel: str = unitLabel + + +class Pressure(Enum): + PA = Unit(1.0, 0.0, "Pa") + KPA = Unit(1e-3, 0.0, "kPa") + MPA = Unit(1e-6, 0.0, "MPa") + GPA = Unit(1e-9, 0.0, "GPa") + BAR = Unit(1.0e-5, 0.0, "Bar") + PSI = Unit(0.00015, 0.0, "psi") + + +class Length(Enum): + METER = Unit(1.0, 0.0, "m") + KILOMETER = Unit(1e-3, 0.0, "km") + FEET = Unit(3.28084, 0.0, "ft") + MILE = Unit(0.00062, 0.0, "mile") + + +class Volume(Enum): + CUBIC_METER = Unit(1.0, 0.0, "m3") + CUBIC_FEET = Unit(35.31467, 0.0, "ft3") + BBL = Unit(6.28981, 0.0, "bbl") + + +class Mass(Enum): + KG = Unit(1.0, 0.0, "kg") + TON = Unit(1e-3, 0.0, "ton") + MEGATON = Unit(1e-6, 0.0, "Mton") + POUND = Unit(2.20462, 0.0, "lb") + + +class Density(Enum): + KG_PER_CUBIC_METER = Unit(1.0, 0.0, "kg/m3") + G_PER_CUBIC_CENTIMETER = Unit(0.001, 0.0, "g/cm3") + POUND_PER_BBL = Unit(0.35051, 0.0, "lb/bbl") + + +class VolumetricRate(Enum): + CUBIC_METER_PER_SECOND = Unit(1.0, 0.0, "m3/s") + CUBIC_METER_PER_HOUR = Unit(3600.0, 0.0, "m3/h") + CUBIC_METER_PER_DAY = Unit(86400.0, 0.0, "m3/day") + BBL_PER_DAY = Unit(54343.962, 0.0, "bbl/day") + + +class MassRate(Enum): + KG_PER_SECOND = Unit(1.0, 0.0, "kg/s") + KG_PER_HOUR = Unit(3600.0, 0.0, "kg/h") + KG_PER_DAY = Unit(86400.0, 0.0, "kg/day") + TON_PER_DAY = Unit(86.4, 0.0, "ton/day") + MTPA = Unit(0.0315576, 0.0, "MTPA") + + +class Time(Enum): + SECOND = Unit(1.0, 0.0, "s") + HOUR = Unit(0.00028, 0.0, "h") + DAY = Unit(1.1574e-5, 0.0, "day") + MONTH = Unit(3.80263e-7, 0.0, "month") + YEAR = Unit(3.1688e-8, 0.0, "year") + + +class Permeability(Enum): + SQUARE_METER = Unit(1.0, 0.0, "m2") + DARCY = Unit(1e12, 0.0, "D") + MILLI_DARCY = Unit(1e15, 0.0, "mD") + + +class Temperature(Enum): + K = Unit(1.0, 0.0, "K") + CELSIUS = Unit(1.0, 273.15, "C") + FAHRENHEIT = Unit(1.8, -459.67, "F") + + +class NoUnit(Enum): + SAME = Unit(1.0, 0.0, "") + + +associationPropertyUnitEnum: dict[str, Enum] = { + "pressure": cast(Enum, Pressure), + "bhp": cast(Enum, Pressure), + "stress": cast(Enum, Pressure), + "length": cast(Enum, Length), + "volumetricRate": cast(Enum, VolumetricRate), + "massRate": cast(Enum, MassRate), + "volume": cast(Enum, Volume), + "mass": cast(Enum, Mass), + "density": cast(Enum, Density), + "temperature": cast(Enum, Temperature), + "time": cast(Enum, Time), + "permeability": cast(Enum, Permeability), + "nounit": cast(Enum, NoUnit), +} + + +def getPropertyUnitEnum(propertyName: str) -> Enum: + """Get the Unit enum from property name. + + Args: + propertyName (str): name of the property. + + Returns: + Enum: Unit enum. + """ + return associationPropertyUnitEnum[propertyName] + + +def getSIUnits() -> dict[str, Unit]: + """Get the dictionary of property Names:Units. + + Generates a dict where the keys are meta-properties + like pressure, mass etc ... and where the values are Unit + composed of a conversion factor and its unit associated. + Here, the conversion factor will always be 1.0 and the unit will + be the SI associate because we work with SI units. + + Returns: + dict[str, Unit]: dictionary of unit names as keys and Unit enum as value. + """ + return { + "pressure": Pressure.PA.value, + "bhp": Pressure.PA.value, + "stress": Pressure.PA.value, + "length": Length.METER.value, + "volumetricRate": VolumetricRate.CUBIC_METER_PER_SECOND.value, + "massRate": MassRate.KG_PER_SECOND.value, + "volume": Volume.CUBIC_METER.value, + "mass": Mass.KG.value, + "density": Density.KG_PER_CUBIC_METER.value, + "temperature": Temperature.K.value, + "time": Time.SECOND.value, + "permeability": Permeability.SQUARE_METER.value, + "nounit": NoUnit.SAME.value, + } + + +def convert(number: float, unitObj: Unit) -> float: + """Converts a float number that has SI unit to a specific unit. + + Args: + number (float): Number to convert. + unitObj (Unit): Object containing conversion multiplier and adder. + + Returns: + float: number converted to the correct unit. + """ + return number * unitObj.conversionMultiplier + unitObj.conversionAdder + + +def enumerationDomainUnit(enumObj: Enum) -> str: + """Get the xml code corresponding to unit enum object for drop down list. + + Args: + enumObj (Enum): Unit enum object. + + Returns: + str: xml text. + """ + xml: str = """""" + for i, unitObj in enumerate(list(enumObj)): # type: ignore[call-overload] + unit: Unit = unitObj.value + assert isinstance(unit, Unit), "enumObj does not contain Unit objects." + xml += f"""""" + xml += """""" + return xml diff --git a/geos-posp/src/geos_posp/utils/geosUtils.py b/geos-posp/src/geos_posp/utils/geosUtils.py new file mode 100644 index 00000000..20eed657 --- /dev/null +++ b/geos-posp/src/geos_posp/utils/geosUtils.py @@ -0,0 +1,109 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +import numpy as np +import numpy.typing as npt + +__doc__ = """ +GeosUtils module defines usefull methods to process GEOS outputs according to +GEOS conventions. +""" + + +def getAttributeMatrixFromVector( + attrArray: npt.NDArray[np.float64], +) -> npt.NDArray[np.float64]: + r"""Get the matrix of attribute values from the vector. + + Matrix to vector conversion is the following: + + * if input vector size is 3: + .. math:: + + (v1, v2, v3) => \begin{bmatrix} + v0 & 0 & 0 \\ + 0 & v1 & 0 \\ + 0 & 0 & v2 + \end{bmatrix} + + * if input vector size is 6: + .. math:: + + (v1, v2, v3, v4, v5, v6) => \begin{bmatrix} + v1 & v6 & v5 \\ + v6 & v2 & v4 \\ + v5 & v4 & v3 + \end{bmatrix} + + + .. WARNING:: Input vector must be of size 3 or 6. + + Args: + attrArray (npt.NDArray[np.float64]): Vector of attribute values. + + Returns: + npt.NDArray[np.float64]: matrix of attribute values + + """ + assert attrArray.size > 2, ( + "Vectorial attribute must contains at least " + "3 components." + ) + # diagonal terms + matrix: npt.NDArray[np.float64] = np.diagflat(attrArray[:3]) + # shear stress components + if attrArray.size == 6: + matrix[0, 1] = attrArray[5] + matrix[1, 0] = attrArray[5] + + matrix[0, 2] = attrArray[4] + matrix[2, 0] = attrArray[4] + + matrix[1, 2] = attrArray[3] + matrix[2, 1] = attrArray[3] + return matrix + + +def getAttributeVectorFromMatrix( + attrMatrix: npt.NDArray[np.float64], size: int +) -> npt.NDArray[np.float64]: + r"""Get the vector of attribute values from the matrix. + + Matrix to vector conversion is the following: + + * 3x3 diagonal matrix: + .. math:: + + \begin{bmatrix} + M00 & 0 & 0 \\ + 0 & M11 & 0 \\ + 0 & 0 & M22 + \end{bmatrix} + => (M00, M11, M22) + + * otherwise: + .. math:: + + \begin{bmatrix} + M00 & M01 & M02 \\ + M01 & M11 & M12 \\ + M02 & M12 & M22 + \end{bmatrix} + => (M00, M11, M22, M12, M02, M01) + + Args: + attrMatrix (npt.NDArray[np.float64]): Matrix of attribute values. + size (int): Size of the final vector. + + Returns: + npt.NDArray[np.float64]: vector of attribute values + + """ + attrArray: npt.NDArray[np.float64] = np.full(size, np.nan) + # diagonal terms + attrArray[:3] = np.diag(attrMatrix) + # shear stress components + if attrArray.size == 6: + attrArray[3] = attrMatrix[1, 2] + attrArray[4] = attrMatrix[0, 2] + attrArray[5] = attrMatrix[0, 1] + return attrArray diff --git a/geos-posp/src/geos_posp/visu/PVUtils/DisplayOrganizationParaview.py b/geos-posp/src/geos_posp/visu/PVUtils/DisplayOrganizationParaview.py new file mode 100644 index 00000000..8e8f3f96 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/PVUtils/DisplayOrganizationParaview.py @@ -0,0 +1,208 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +from typing import Any + +from paraview.simple import ( # type: ignore[import-not-found] + AssignViewToLayout, + CreateLayout, + CreateView, + Delete, + GetLayoutByName, + GetLayouts, + GetViews, + GetViewsInLayout, + RemoveLayout, + SetActiveView, +) +from typing_extensions import Self + + +def buildNewLayoutWithPythonView() -> Any: # noqa: ANN401 + """Create a new PythonView layout.""" + # create a new layout + organization: DisplayOrganizationParaview = DisplayOrganizationParaview() + layout_names: list[str] = organization.getLayoutsNames() + nb_layouts: int = len(layout_names) + layoutName: str = "Layout #" + str(nb_layouts + 1) + # increment layout index until the layout name is a new one + cpt: int = 1 + while layoutName in layout_names: + layoutName = "Layout #" + str(nb_layouts + cpt) + cpt += 1 + organization.addLayout(layoutName) + + # add a new python view to the layout + organization.addViewToLayout("PythonView", layoutName, 0) + return organization.getLayoutViews()[layoutName][0] + + +class DisplayOrganizationParaview: + """Object to manage Paraview layouts.""" + + def __init__(self: Self) -> None: + """Keeps track of Paraview layouts and views when created or removed.""" + self._layouts_keys: list[Any] = [] + self._layout_names: list[str] = [] + self._views_cpt: int = 0 + self._layout_views: dict[str, Any] = {} + self._views_name: dict[str, Any] = {} + self.initLayouts() + self.initLayoutViews() + + def initLayouts(self: Self) -> None: + """Initialize layouts.""" + self._layouts_keys = list(GetLayouts().keys()) + self._layouts_names = [] + for layout_tuple in self._layouts_keys: + self._layouts_names.append(layout_tuple[0]) + + def getLayoutsKeys(self: Self) -> list[Any]: + """Get layout keys. + + Returns: + list[Any]: list of layout keys. + """ + return self._layouts_keys + + def getLayoutsNames(self: Self) -> list[str]: + """Get layout names. + + Returns: + list[str]: list of layout names. + """ + return self._layouts_names + + def getNumberLayouts(self: Self) -> int: + """Get the number of layouts. + + Returns: + int: number of layouts. + """ + return len(self._layouts_keys) + + def getViewsCpt(self: Self) -> int: + """Get the number of views. + + Returns: + int: number of views. + """ + return self._views_cpt + + def addOneToCpt(self: Self) -> None: + """Increment number of views.""" + self._views_cpt += 1 + + def initLayoutViews(self: Self) -> None: + """Initialize layout views.""" + self._views_name = {} + self._layout_views = {} + all_views: list[Any] = GetViews() + layouts_keys: list[Any] = self.getLayoutsKeys() + layout_names: list[str] = self.getLayoutsNames() + for i in range(self.getNumberLayouts()): + self._layout_views[layout_names[i]] = [] + views_in_layout = GetViewsInLayout(GetLayouts()[layouts_keys[i]]) + for view in all_views: + if view in views_in_layout: + self._layout_views[layout_names[i]].append(view) + name_view: str = "view" + str(self.getViewsCpt()) + self._views_name[name_view] = view + self.addOneToCpt() + + def getLayoutViews(self: Self) -> dict[str, Any]: + """Get layout views. + + Returns: + dict[Any:Any]: dictionnary of layout views. + """ + return self._layout_views + + def getViewsName(self: Self) -> dict[str, Any]: + """Get view names. + + Returns: + list[str]: list of view names. + """ + return self._views_name + + def updateOrganization(self: Self) -> None: + """Update layouts.""" + self._views_cpt = 0 + self.initLayouts() + self.initLayoutViews() + + def addLayout(self: Self, new_layout_name: str) -> None: + """Add a layout. + + Args: + new_layout_name (str): name of the new layout. + """ + if new_layout_name not in self.getLayoutsNames(): + CreateLayout(new_layout_name) + else: + print( + f'This layout name "{new_layout_name}" is already used, please pick a new one.\n' + ) + self.updateOrganization() + + def removeLayout(self: Self, layout_name: str) -> None: + """Remove a layout. + + Args: + layout_name (str): name of the layout to remove. + """ + if layout_name not in self.getLayoutsNames(): + RemoveLayout(GetLayoutByName(layout_name)) + else: + print(f'This layout name "{layout_name}" does not exist.') + self.updateOrganization() + + def addViewToLayout( + self: Self, viewType: str, layout_name: str, position: int + ) -> None: + """Add a view to a layout. + + Args: + viewType (str): type of view. + layout_name (str): name of the layout. + position (int): position of the view. + """ + SetActiveView(None) + layout_to_use = GetLayoutByName(layout_name) + new_view = CreateView(viewType) + AssignViewToLayout(view=new_view, layout=layout_to_use, hint=position) + self.updateOrganization() + + def RemoveViewFromLayout( + self: Self, view_name: str, layout_name: str, position: int + ) -> None: + """Remove a view from a layout. + + Args: + view_name (str): name of view. + layout_name (str): name of the layout. + position (int): position of the view. + """ + views_name: dict[str, Any] = self.getViewsName() + view_to_delete = views_name[view_name] + SetActiveView(view_to_delete) + Delete(view_to_delete) + del view_to_delete + layout_to_use = GetLayoutByName(layout_name) + layout_to_use.Collapse(position) + self.updateOrganization() + + def SwapCellsInLayout( + self: Self, layout_name: str, position1: int, position2: int + ) -> None: + """Swap views in a layout. + + Args: + layout_name (str): name of the layout. + position1 (int): first position of the view. + position2 (int): second position of the view. + """ + layout_to_use = GetLayoutByName(layout_name) + layout_to_use.SwapCells(position1, position2) diff --git a/geos-posp/src/geos_posp/visu/PVUtils/__init__.py b/geos-posp/src/geos_posp/visu/PVUtils/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/visu/PVUtils/checkboxFunction.py b/geos-posp/src/geos_posp/visu/PVUtils/checkboxFunction.py new file mode 100644 index 00000000..7fce5261 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/PVUtils/checkboxFunction.py @@ -0,0 +1,22 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa +# type: ignore +def createModifiedCallback(anobject): + """Helper for the creation and use of vtkDataArraySelection in ParaView. + + Args: + anobject: any object. + """ + import weakref + + weakref_obj = weakref.ref(anobject) + anobject = None + + def _markmodified(*args, **kwars): + o = weakref_obj() + if o is not None: + o.Modified() + + return _markmodified diff --git a/geos-posp/src/geos_posp/visu/PVUtils/matplotlibOptions.py b/geos-posp/src/geos_posp/visu/PVUtils/matplotlibOptions.py new file mode 100644 index 00000000..a1db5c6b --- /dev/null +++ b/geos-posp/src/geos_posp/visu/PVUtils/matplotlibOptions.py @@ -0,0 +1,87 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file + +from enum import Enum + +from typing_extensions import Self + + +class OptionSelectionEnum(Enum): + def __init__(self: Self, displayName: str, optionValue: str) -> None: + """Define the enumeration to options for Paraview selectors. + + Args: + displayName (str): name displayed in the selector + optionValue (str): value used by matplotlib. + + Defaults to None (same optionName as displayName) + """ + self.displayName: str = displayName + self.optionValue: str = optionValue + + +class LegendLocationEnum(OptionSelectionEnum): + BEST = ("best", "best") + UPPER_LEFT = ("upper left", "upper left") + UPPER_CENTER = ("upper center", "upper center") + UPPER_RIGHT = ("upper right", "upper right") + CENTER_LEFT = ("center left", "center left") + CENTER = ("center", "center") + CENTER_RIGHT = ("center right", "center right") + LOWER_LEFT = ("lower left", "lower left") + LOWER_CENTER = ("lower center", "lower center") + LOWER_RIGHT = ("lower right", "lower right") + + +class FontStyleEnum(OptionSelectionEnum): + NORMAL = ("normal", "normal") + ITALIC = ("italic", "italic") + OBLIQUE = ("oblique", "oblique") + + +class FontWeightEnum(OptionSelectionEnum): + NORMAL = ("normal", "normal") + BOLD = ("bold", "bold") + HEAVY = ("heavy", "heavy") + LIGHT = ("light", "light") + + +class LineStyleEnum(OptionSelectionEnum): + NONE = ("None", "None") + SOLID = ("solid", "-") + DASHED = ("dashed", "--") + DASHDOT = ("dashdot", "-.") + DOTTED = ("dotted", ":") + + +class MarkerStyleEnum(OptionSelectionEnum): + NONE = ("None", "") + POINT = ("point", ".") + CIRCLE = ("circle", "o") + TRIANGLE = ("triangle", "^") + SQUARE = ("square", "s") + STAR = ("star", "*") + DIAMOND = ("diamond", "D") + PLUS = ("plus", "+") + X = ("x", "x") + + +def optionEnumToXml(enumObj: OptionSelectionEnum) -> str: + """Creates an enumeration domain from an OptionSelectionEnum object. + + Dedicated to the dropdown widgets of paraview plugin. + + Args: + enumObj (OptionSelectionEnum): Enumeration values to put in the dropdown + widget. + + Returns: + str: the XML string. + """ + xml: str = """""" + for i, unitObj in enumerate(list(enumObj)): # type: ignore[call-overload] + xml += f"""""" + xml += """""" + return xml diff --git a/geos-posp/src/geos_posp/visu/PVUtils/paraviewTreatments.py b/geos-posp/src/geos_posp/visu/PVUtils/paraviewTreatments.py new file mode 100644 index 00000000..7de0995b --- /dev/null +++ b/geos-posp/src/geos_posp/visu/PVUtils/paraviewTreatments.py @@ -0,0 +1,611 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +from enum import Enum +from typing import Any, Union + +import numpy as np +import numpy.typing as npt +import pandas as pd # type: ignore[import-untyped] +from paraview.modules.vtkPVVTKExtensionsMisc import ( # type: ignore[import-not-found] + vtkMergeBlocks, +) +from paraview.simple import ( # type: ignore[import-not-found] + FindSource, + GetActiveView, + GetAnimationScene, + GetDisplayProperties, + GetSources, + servermanager, +) +from vtkmodules.vtkCommonCore import ( + vtkDataArray, + vtkDataArraySelection, + vtkDoubleArray, + vtkPoints, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCompositeDataSet, + vtkDataObject, + vtkMultiBlockDataSet, + vtkPolyData, + vtkTable, + vtkUnstructuredGrid, +) + +from geos_posp.processing.vtkUtils import ( + getArrayInObject, + isAttributeInObject, +) +from geos_posp.utils.GeosOutputsConstants import ( + ComponentNameEnum, + GeosMeshOutputsEnum, +) + +# valid sources for Python view configurator +# TODO: need to be consolidated +HARD_CODED_VALID_PVC_TYPE: set[str] = {"GeosLogReader", "RenameArrays"} + + +def vtkTableToDataframe(table: vtkTable) -> pd.DataFrame: + """From a vtkTable, creates and returns a pandas dataframe. + + Args: + table (vtkTable): vtkTable object. + + Returns: + pd.DataFrame: Pandas dataframe. + """ + data: list[dict[str, Any]] = [] + for rowIndex in range(table.GetNumberOfRows()): + rowData: dict[str, Any] = {} + for colIndex in range(table.GetNumberOfColumns()): + colName: str = table.GetColumnName(colIndex) + cellValue: Any = table.GetValue(rowIndex, colIndex) + # we have a vtkVariant value, we need a float + cellValueF: float = cellValue.ToFloat() + rowData[colName] = cellValueF + data.append(rowData) + df: pd.DataFrame = pd.DataFrame(data) + return df + + +def vtkPolyDataToPointsDataframe(polydata: vtkPolyData) -> pd.DataFrame: + """Creates a pandas dataframe containing points data from vtkPolyData. + + Args: + polydata (vtkPolyData): vtkPolyData object. + + Returns: + pd.DataFrame: Pandas dataframe containing the points data. + """ + points: vtkPoints = polydata.GetPoints() + assert points is not None, "Points is undefined." + nbrPoints: int = points.GetNumberOfPoints() + data: dict[str, Any] = { + "Point ID": np.empty(nbrPoints), + "PointsX": np.empty(nbrPoints), + "PointsY": np.empty(nbrPoints), + "PointsZ": np.empty(nbrPoints), + } + for pointID in range(nbrPoints): + point: tuple[float, float, float] = points.GetPoint(pointID) + data["Point ID"][pointID] = pointID + data["PointsX"][pointID] = point[0] + data["PointsY"][pointID] = point[1] + data["PointsZ"][pointID] = point[2] + pointData = polydata.GetPointData() + nbrArrays: int = pointData.GetNumberOfArrays() + for i in range(nbrArrays): + arrayToUse = pointData.GetArray(i) + arrayName: str = pointData.GetArrayName(i) + subArrayNames: list[str] = findSubArrayNames(arrayToUse, arrayName) + # Collect the data for each sub array + for ind, name in enumerate(subArrayNames): + data[name] = np.empty(nbrPoints) + for k in range(nbrPoints): + # Every element of the tuple correspond to one distinct + # sub array so we only need one value at a time + value: float = arrayToUse.GetTuple(k)[ind] + data[name][k] = value + df: pd.DataFrame = pd.DataFrame(data).set_index("Point ID") + return df + + +def vtkUnstructuredGridCellsToDataframe(grid: vtkUnstructuredGrid) -> pd.DataFrame: + """Creates a pandas dataframe containing points data from vtkUnstructuredGrid. + + Args: + grid (vtkUnstructuredGrid): vtkUnstructuredGrid object. + + Returns: + pd.DataFrame: Pandas dataframe. + """ + cellIdAttributeName = GeosMeshOutputsEnum.VTK_ORIGINAL_CELL_ID.attributeName + cellData = grid.GetCellData() + numberCells: int = grid.GetNumberOfCells() + data: dict[str, Any] = {} + for i in range(cellData.GetNumberOfArrays()): + arrayToUse = cellData.GetArray(i) + arrayName: str = cellData.GetArrayName(i) + subArrayNames: list[str] = findSubArrayNames(arrayToUse, arrayName) + # Collect the data for each sub array + for ind, name in enumerate(subArrayNames): + data[name] = np.empty(numberCells) + for k in range(numberCells): + # Every element of the tuple correspond to one distinct + # sub array so we only need one value at a time + value: float = arrayToUse.GetTuple(k)[ind] + data[name][k] = value + df: pd.DataFrame = pd.DataFrame(data).astype({cellIdAttributeName: int}) + + # set cell ids as index + + # df = df.astype({cellIdAttributeName: int}) + return df.set_index(cellIdAttributeName) + + +def vtkToDataframe(dataset: vtkDataObject) -> pd.DataFrame: + """Creates a dataframe containing points data from vtkTable or vtkPolyData. + + Args: + dataset (Any): dataset to convert if possible. + + Returns: + pd.DataFrame: if the dataset is in the right format. + """ + if isinstance(dataset, vtkTable): + return vtkTableToDataframe(dataset) + elif isinstance(dataset, vtkPolyData): + return vtkPolyDataToPointsDataframe(dataset) + elif isinstance(dataset, vtkUnstructuredGrid): + return vtkUnstructuredGridCellsToDataframe(dataset) + else: + raise AssertionError( + f"Invalid dataset format {type(dataset)}. " + + "Supported formats are: vtkTable, vtkpolyData and vtkUnstructuredGrid" + ) + + +def findSubArrayNames(vtkArray: vtkDataArray, arrayName: str) -> list[str]: + """Get sub array names from multi array attributes. + + Because arrays in ParaView can be of multiple dimensions, + it can be difficult to convert these arrays to numpy arrays. + Therefore, we can split the original array into multiple sub + one dimensional arrays. In that case, new sub names need to be + derived from the original array to be used. + + Args: + vtkArray (vtkDataArray): Array from vtk library. + arrayName (str): Name of the array. + + Returns: + list[str]: Sub array names from original array name. + """ + # The ordering of six elements can seem odd but is adapted to + # Geos output format of stress as : + # sigma11, sigma22, sigma33, sigma23, sigma13, sigma12 + sixComponents: tuple[str, str, str, str, str, str] = ComponentNameEnum.XYZ.value + nbrComponents: int = vtkArray.GetNumberOfComponents() + subArrayNames: list[str] = [] + if nbrComponents == 1: + subArrayNames.append(arrayName) + elif nbrComponents < 6: + for j in range(nbrComponents): + subArrayNames.append(arrayName + "_" + sixComponents[j]) + else: + for j in range(nbrComponents): + subArrayNames.append(arrayName + "_" + str(j)) + return subArrayNames + + +def getDataframesFromMultipleVTKSources( + sourceNames: set[str], commonColumn: str +) -> list[pd.DataFrame]: + """Creates the dataframe from each source if they have the commonColumn. + + Args: + sourceNames (set[str]): list of sources. + commonColumn (str): common column name. + + Returns: + list[pd.DataFrame]: output dataframe. + """ + # indexSource: int = commonColumn.rfind("__") + # commonColumnNoSource: str = commonColumn[:indexSource] + validDataframes: list[pd.DataFrame] = [] + for name in sourceNames: + source = FindSource(name) + assert source is not None, "Source is undefined." + dataset = servermanager.Fetch(source) + assert dataset is not None, "Dataset is undefined." + currentDF: pd.DataFrame = vtkToDataframe(dataset) + if commonColumn in currentDF.columns: + dfModified = currentDF.rename( + columns={ + col: col + "__" + name + for col in currentDF.columns + if col != commonColumn + } + ) + validDataframes.append(dfModified) + else: + print( + f"The source <<{name}>> could not be used" + + " to plot because the variable named <<" + + f"{commonColumn}>> could not be found." + ) + return validDataframes + + +def mergeDataframes(dataframes: list[pd.DataFrame], commonColumn: str) -> pd.DataFrame: + """Merge all dataframes into a single one by using the common column. + + Args: + dataframes (list[pd.DataFrame]): List of dataframes from + getDataframesFromMultipleVTKSources. + commonColumn (str): Name of the only common column between + all of the dataframes. + + Returns: + pd.DataFrame: Merged dataframes into a single one by 'outer' + on the commonColumn. + """ + assert len(dataframes) > 0 + if len(dataframes) == 1: + return dataframes[0] + else: + df0: pd.DataFrame = dataframes[0] + df1: pd.DataFrame = dataframes[1] + merged: pd.DataFrame = df0.merge(df1, on=commonColumn, how="outer") + if len(dataframes) > 2: + for df in dataframes[2:]: + merged = merged.merge(df, on=commonColumn, how="outer") + return merged + + +def addDataframeColumnsToVtkPolyData( + polyData: vtkPolyData, df: pd.DataFrame +) -> vtkPolyData: + """Add columns from a dataframe to a vtkPolyData. + + Args: + polyData (vtkPolyData): vtkPolyData before modifcation. + df (pd.DataFrame): Pandas dataframe. + + Returns: + vtkPolyData: vtkPolyData with new arrays. + """ + for column_name in df.columns: + column = df[column_name].values + array = vtkDoubleArray() + array.SetName(column_name) + array.SetNumberOfValues(polyData.GetNumberOfPoints()) + for i in range(polyData.GetNumberOfPoints()): + array.SetValue(i, column[i]) + polyData.GetPointData().AddArray(array) + + # Update vtkPolyData object + polyData.GetPointData().Modified() + polyData.Modified() + return polyData + + +# Functions to help the processing of PythonViewConfigurator + + +def getPossibleSourceNames() -> set[str]: + """Get the list of valid source names for PythonViewConfigurator. + + In PythonViewConfigurator, multiple sources can be considered as + valid inputs. We want the user to know the names of every of these + sources that can be used to plot data. This function therefore identifies + which source names are valid to be used later as sources. + + Returns: + set[str]: Source names in the paraview pipeline. + """ + # get all sources different from PythonViewConfigurator + validNames: set[str] = set() + for k in GetSources(): + sourceName: str = k[0] + source = FindSource(sourceName) + if (source is not None) and ("PythonViewConfigurator" not in source.__str__()): + dataset = servermanager.Fetch(source) + if dataset.IsA("vtkPolyData") or dataset.IsA("vtkTable"): + validNames.add(sourceName) + return validNames + + +def usefulSourceNamesPipeline() -> set[str]: + """Get the list of valid pipelines for PythonViewConfigurator. + + When using the PythonViewConfigurator, we want to check if the sources + in the ParaView pipeline are compatible with what the filter can take as + input. So this function scans every sources of the pipeline and if it + corresponds to one of the hardcoded valid types, we keep the name. + They are right now : ["GeosLogReader", "RenameArrays"] + + Returns: + set[str]: [sourceName1, ..., sourceNameN] + """ + usefulSourceNames: set[str] = set() + allSourceNames: set[str] = {n[0] for n, s in GetSources().items()} + for name in allSourceNames: + source = FindSource(name) + if type(source).__name__ in HARD_CODED_VALID_PVC_TYPE: + usefulSourceNames.add(name) + return usefulSourceNames + + +def getDatasFromSources(sourceNames: set[str]) -> dict[str, pd.DataFrame]: + """Get the data from input sources. + + Args: + sourceNames (set[str]): [sourceName1, ..., sourceNameN] + + Returns: + dict[[str, pd.DataFrame]]: dictionary where source names are keys and + dataframe are values. + { sourceName1: servermanager.Fetch(FindSource(sourceName1)), + ... + sourceNameN: servermanager.Fetch(FindSource(sourceNameN)) } + """ + usefulDatas: dict[str, Any] = {} + for name in sourceNames: + dataset = servermanager.Fetch(FindSource(name)) + usefulDatas[name] = dataset + return usefulDatas + + +def usefulVisibleDatasPipeline() -> dict[str, Any]: + """Get the list of visible pipelines. + + When using the PythonViewConfigurator, we want to collect the data of + each source that is visible in the paraview pipeline and that is + compatible as input data for the filter. Therefore, only certain types of + sources will be considered as valid. They are right now : + ["GeosLogReader", "RenameArrays"] + + Finally, if the sources are visible and valid, we access their data and + return the names of the source and their respective data. + + Returns: + dict[str, 'vtkInformation']: dictionary of source names and data from + pipeline. + { sourceName1: servermanager.Fetch(FindSource(sourceName1)), + ... + sourceNameN: servermanager.Fetch(FindSource(sourceNameN)) } + """ + usefulDatas: dict[str, Any] = {} + sourceNamesVisible: set[str] = set() + for n, s in GetSources().items(): + if servermanager.GetRepresentation(s, GetActiveView()) is not None: + displayProperties = GetDisplayProperties(s, view=GetActiveView()) + if (displayProperties is not None) and (displayProperties.Visibility == 1): + sourceNamesVisible.add(n[0]) + + for name in sourceNamesVisible: + source = FindSource(name) + if type(source).__name__ in HARD_CODED_VALID_PVC_TYPE: + usefulDatas[name] = servermanager.Fetch(FindSource(name)) + return usefulDatas + + +def isFilter(sourceName: str) -> bool: + """Identify if a source name can link to a filter in the ParaView pipeline. + + Args: + sourceName (str): name of a source object in the pipeline + + Returns: + bool: True if filter, False instead. + """ + source: Any = FindSource(sourceName) + if source is None: + print(f"sourceName <<{sourceName}>> does not exist in the pipeline") + return False + else: + try: + test: Any = source.GetClientSideObject().GetInputAlgorithm() # noqa: F841 + return True + except Exception: + return False + + +def getFilterInput(sourceName: str) -> vtkDataObject: + """Access the vtk dataset that is used as input for a filter. + + Args: + sourceName (str): name of a source object in the pipeline. + + Returns: + Any: The vtk dataset that serves as input for the filter. + """ + filtre = FindSource(sourceName) + assert filtre is not None, "Source is undefined." + clientSideObject = filtre.GetClientSideObject() + assert clientSideObject is not None, "Client Side Object is undefined." + inputAlgo = clientSideObject.GetInputAlgorithm() + assert inputAlgo is not None, "Input Algorithm is undefined." + inputValues = inputAlgo.GetInput() + if isinstance(inputValues, vtkDataObject): + return inputValues + return vtkDataObject() + + +def getArrayChoices(array: vtkDataArraySelection) -> list[str]: + """Extracts the column names of input array when they are enabled. + + Args: + array (vtkDataArraySelection): input data + + Returns: + set[str]: [columnName1, ..., columnNameN] + """ + checkedColumns: list[str] = [] + for i in range(array.GetNumberOfArrays()): + columnName: str = array.GetArrayName(i) + if array.ArrayIsEnabled(columnName): + checkedColumns.append(columnName) + return checkedColumns + + +def integrateSourceNames(sourceNames: set[str], arrayChoices: set[str]) -> set[str]: + """Aggregate source and arrayChoices names. + + When creating the user choices in PythonViewConfigurator, you need + to take into account both the source names and the choices of curves + to have user choices corresponding to the column names of the dataframe + with the data to be plot. + + Args: + sourceNames (set[str]): Name of sources found in ParaView pipeline. + arrayChoices (set[str]): Column names of the vtkdataarrayselection. + + Returns: + set[str]: [sourceName1__choice1, sourceName1__choice2, + ..., sourceNameN__choiceN] + """ + completeNames: set[str] = set() + for sourceName in sourceNames: + for choice in arrayChoices: + completeName: str = choice + "__" + sourceName + completeNames.add(completeName) + return completeNames + + +def getVtkOriginalCellIds( + mesh: Union[vtkMultiBlockDataSet, vtkCompositeDataSet, vtkDataObject] +) -> list[str]: + """Get vtkOriginalCellIds from a vtkUnstructuredGrid object. + + Args: + mesh (vtkMultiBlockDataSet|vtkCompositeDataSet|vtkDataObject): input mesh. + + Returns: + list[str]: ids of the cells. + """ + # merge blocks for vtkCompositeDataSet + mesh2: vtkUnstructuredGrid = mergeFilterPV(mesh, True) + name: str = GeosMeshOutputsEnum.VTK_ORIGINAL_CELL_ID.attributeName + assert isAttributeInObject( + mesh2, name, False + ), f"Attribute {name} is not in the mesh." + return [str(int(ide)) for ide in getArrayInObject(mesh2, name, False)] + + +def strEnumToEnumerationDomainXml(enumObj: Enum) -> str: + """Creates an enumeration domain from an Enum objec. + + Creates an enumeration domain from an Enum objec + for the dropdown widgets of paraview plugin. + + Args: + enumObj (Enum): Enumeration values to put in the dropdown widget. + + Returns: + str: the XML string. + """ + xml: str = """""" + for i, unitObj in enumerate(list(enumObj)): # type: ignore[call-overload] + xml += f"""""" + xml += """""" + return xml + + +def strListToEnumerationDomainXml(properties: Union[list[str], set[str]]) -> str: + """Creates an enumeration domain from a list of strings. + + Creates an enumeration domain from a list of strings + for the dropdown widgets of paraview plugin. + + Args: + properties (set[str] | list[str]): Properties to put in the dropdown widget. + + Returns: + str: the XML string. + """ + xml: str = """""" + for i, prop in enumerate(list(properties)): + xml += f"""""" + xml += """""" + return xml + + +def dataframeForEachTimestep(sourceName: str) -> dict[str, pd.DataFrame]: + """Get the data from source at each time step. + + In ParaView, a source object can contain data for multiple + timesteps. If so, knowing the source name, we can access its data + for each timestep and store it in a dict where the keys are the + timesteps and the values the data at each one of them. + + Args: + sourceName (str): Name of the source in ParaView pipeline. + + Returns: + dict[str, pd.DataFrame]: dictionary where time is the key and dataframe + is the value. + """ + animationScene = GetAnimationScene() + assert animationScene is not None, "animationScene is undefined." + # we set the animation to the initial timestep + animationScene.GoToFirst() + source = FindSource(sourceName) + dataset: vtkDataObject = servermanager.Fetch(source) + assert dataset is not None, f"Dataset is undefined." + dataset2: vtkUnstructuredGrid = mergeFilterPV(dataset) + time: str = str(animationScene.TimeKeeper.Time) + dfPerTimestep: dict[str, pd.DataFrame] = {time: vtkToDataframe(dataset2)} + # then we iterate on the other timesteps of the source + for _ in range(animationScene.NumberOfFrames): # type: ignore + animationScene.GoToNext() + source = FindSource(sourceName) + dataset = servermanager.Fetch(source) + dataset2 = mergeFilterPV(dataset) + time = str(animationScene.TimeKeeper.Time) + dfPerTimestep[time] = vtkToDataframe(dataset2) + return dfPerTimestep + + +def getTimeStepIndex(time: float, timeSteps: npt.NDArray[np.float64]) -> int: + """Get the time step index of input time from the list of time steps. + + Args: + time (float): time + timeSteps (npt.NDArray[np.float64]): Array of time steps + + Returns: + int: time step index + """ + indexes: npt.NDArray[np.int64] = np.where(np.isclose(timeSteps, time))[0] + assert ( + indexes.size > 0 + ), f"Current time {time} does not exist in the selected object." + return int(indexes[0]) + + +def mergeFilterPV( + input: vtkDataObject, + keepPartialAttributes: bool = False, +) -> vtkUnstructuredGrid: + """Apply Paraview merge block filter. + + Args: + input (vtkMultiBlockDataSet | vtkCompositeDataSet | vtkDataObject): composite + object to merge blocks + keepPartialAttributes (bool): if True, keep partial attributes after merge. + + Defaults to False. + + Returns: + vtkUnstructuredGrid: merged block object + + """ + mergeFilter: vtkMergeBlocks = vtkMergeBlocks() + mergeFilter.SetInputData(input) + mergeFilter.Update() + return mergeFilter.GetOutputDataObject(0) diff --git a/geos-posp/src/geos_posp/visu/__init__.py b/geos-posp/src/geos_posp/visu/__init__.py new file mode 100644 index 00000000..8b137891 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/__init__.py @@ -0,0 +1 @@ + diff --git a/geos-posp/src/geos_posp/visu/mohrCircles/__init__.py b/geos-posp/src/geos_posp/visu/mohrCircles/__init__.py new file mode 100644 index 00000000..4e4c7b57 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/mohrCircles/__init__.py @@ -0,0 +1,3 @@ +MOHR_CIRCLE_PATH: str = "visu/mohrCircles/" +MOHR_CIRCLE_ANALYSIS_MAIN = "mainMohrCircles.py" +MOHR_CIRCLE_EVOLUTION_MAIN = "mainMohrCircleEvolution.py" diff --git a/geos-posp/src/geos_posp/visu/mohrCircles/functionsMohrCircle.py b/geos-posp/src/geos_posp/visu/mohrCircles/functionsMohrCircle.py new file mode 100644 index 00000000..832d8ed5 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/mohrCircles/functionsMohrCircle.py @@ -0,0 +1,169 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +import os +from typing import Any + +import numpy as np +import numpy.typing as npt + +from geos_posp.processing.MohrCircle import MohrCircle +from geos_posp.processing.MohrCoulomb import MohrCoulomb +from geos_posp.visu.mohrCircles import ( + MOHR_CIRCLE_ANALYSIS_MAIN, + MOHR_CIRCLE_PATH, +) + +__doc__ = """ +functionsMohrCircle module provides a set of utilities to instanciate Mohr's +circles and Mohr-Coulomb failure envelope. +""" + + +def buildPythonViewScript( + dir_path: str, + mohrCircles: list[MohrCircle], + rockCohesion: float, + frictionAngle: float, + userChoices: dict[str, Any], +) -> str: + """Builds the Python script used to launch the Python View. + + The script is returned as a string to be then injected in the Python + View. + + Args: + dir_path (str): directory path + + mohrCircles (list[MohrCircle]): list of MohrCircle objects + + rockCohesion (float): rock cohesion (Pa) + + frictionAngle (float): friction angle (rad) + + userChoices (dict[str, Any]): dictionnary of user plot parameters + Returns: + str: Complete Python View script. + """ + pathPythonViewScript: str = os.path.join( + dir_path, MOHR_CIRCLE_PATH, MOHR_CIRCLE_ANALYSIS_MAIN + ) + + mohrCircleParams: list[tuple[str, float, float, float]] = [ + (mohrCircle.getCircleId(), *(mohrCircle.getPrincipalComponents())) + for mohrCircle in mohrCircles + ] + + script: str = "" + script += f"mohrCircleParams = {mohrCircleParams}\n" + script += f"rockCohesion = {rockCohesion}\n" + script += f"frictionAngle = {frictionAngle}\n" + script += f"userChoices = {userChoices}\n\n\n" + with open(pathPythonViewScript) as file: + fileContents = file.read() + script += fileContents + return script + + +def findAnnotateTuples( + mohrCircle: MohrCircle, +) -> tuple[str, str, tuple[float, float], tuple[float, float]]: + """Get the values and location of min and max normal stress or Mohr's circle. + + Args: + mohrCircle (MohrCircle): input Mohr's circle + + maxTau (float): max shear stress + + Returns: + tuple[str, str, tuple[float, float], tuple[float, float]]: labels and + location of labels. + """ + p3, p2, p1 = mohrCircle.getPrincipalComponents() + xMaxDisplay: str = f"{p1:.2E}" + xMinDisplay: str = f"{p3:.2E}" + yPosition: float = 0.0 + xyMax: tuple[float, float] = (p1, yPosition) + xyMin: tuple[float, float] = (p3, yPosition) + return (xMaxDisplay, xMinDisplay, xyMax, xyMin) + + +def getMohrCircleId(cellId: str, timeStep: str) -> str: + """Get Mohr's circle ID from cell id and time step. + + Args: + cellId (str): cell ID + + timeStep (str): time step. + + Returns: + str: Mohr's circle ID + """ + return f"Cell_{cellId}@{timeStep}" + + +def createMohrCircleAtTimeStep( + stressArray: npt.NDArray[np.float64], + cellIds: list[str], + timeStep: str, + convention: bool, +) -> list[MohrCircle]: + """Create MohrCircle object(s) at a given time step for all cell ids. + + Args: + stressArray (npt.NDArray[np.float64]): stress numpy array + + cellIds (list[str]): list of cell ids + + timeStep (str): time step + + convention (bool): convention used for compression. + * False is Geos convention (compression is negative) + * True is usual convention (compression is positive) + + Returns: + list[MohrCircle]: list of MohrCircle objects. + """ + assert stressArray.shape[1] == 6, "Stress vector must be of size 6." + mohrCircles: list[MohrCircle] = [] + sign: float = 1.0 if convention else -1.0 + for i, cellId in enumerate(cellIds): + ide: str = getMohrCircleId(cellId, timeStep) + mohrCircle: MohrCircle = MohrCircle(ide) + mohrCircle.computePrincipalComponents(stressArray[i] * sign) + mohrCircles.append(mohrCircle) + return mohrCircles + + +def createMohrCirclesFromPrincipalComponents( + mohrCircleParams: list[tuple[str, float, float, float]] +) -> list[MohrCircle]: + """Create Mohr's circle objects from principal components. + + Args: + mohrCircleParams (list[tuple[str, float, float, float]]): list of Mohr's + circle parameters + + Returns: + list[MohrCircle]: list of Mohr's circle objects. + """ + mohrCircles: list[MohrCircle] = [] + for circleId, p3, p2, p1 in mohrCircleParams: + mohrCircle: MohrCircle = MohrCircle(circleId) + mohrCircle.setPrincipalComponents(p3, p2, p1) + mohrCircles.append(mohrCircle) + return mohrCircles + + +def createMohrCoulombEnvelope(rockCohesion: float, frictionAngle: float) -> MohrCoulomb: + """Create MohrCoulomb object from user parameters. + + Args: + rockCohesion (float): rock cohesion (Pa). + + frictionAngle (float): friction angle in radian. + + Returns: + MohrCoulomb: MohrCoulomb object. + """ + return MohrCoulomb(rockCohesion, frictionAngle) diff --git a/geos-posp/src/geos_posp/visu/mohrCircles/mainMohrCircles.py b/geos-posp/src/geos_posp/visu/mohrCircles/mainMohrCircles.py new file mode 100644 index 00000000..4b01f874 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/mohrCircles/mainMohrCircles.py @@ -0,0 +1,37 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# type: ignore +try: + import matplotlib.pyplot as plt + from paraview import python_view + + import geos_posp.visu.mohrCircles.functionsMohrCircle as mcf + import geos_posp.visu.mohrCircles.plotMohrCircles as pmc + + plt.close() + + # create MohrCircles + mohrCircles = mcf.createMohrCirclesFromPrincipalComponents( + mohrCircleParams # noqa:F821 + ) + + # create Mohr-Coulomb failure envelope + mohrCoulomb = mcf.createMohrCoulombEnvelope( + rockCohesion, frictionAngle # noqa:F821 + ) + + # plot MohrCircles + fig = pmc.createMohrCirclesFigure( + mohrCircles, mohrCoulomb, userChoices # noqa:F821 + ) + + def setup_data(view) -> None: # noqa + pass + + def render(view, width: int, height: int): # noqa + fig.set_size_inches(float(width) / 100.0, float(height) / 100.0) + return python_view.figure_to_image(fig) + +except Exception as e: + print(e) diff --git a/geos-posp/src/geos_posp/visu/mohrCircles/plotMohrCircles.py b/geos-posp/src/geos_posp/visu/mohrCircles/plotMohrCircles.py new file mode 100644 index 00000000..c3a19d11 --- /dev/null +++ b/geos-posp/src/geos_posp/visu/mohrCircles/plotMohrCircles.py @@ -0,0 +1,273 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +from typing import Any + +import matplotlib.pyplot as plt # type: ignore[import-untyped] +import numpy as np +import numpy.typing as npt +from matplotlib import ticker +from matplotlib.axes import Axes # type: ignore[import-untyped] +from matplotlib.figure import Figure # type: ignore[import-untyped] +from matplotlib.lines import Line2D # type: ignore[import-untyped] + +import geos_posp.visu.mohrCircles.functionsMohrCircle as mcf +from geos_posp.processing.MohrCircle import MohrCircle +from geos_posp.processing.MohrCoulomb import MohrCoulomb +from geos_posp.utils.enumUnits import Pressure, Unit, convert +from geos_posp.utils.GeosOutputsConstants import FAILURE_ENVELOPE +from geos_posp.visu.PVUtils.matplotlibOptions import ( + FontStyleEnum, + FontWeightEnum, + LegendLocationEnum, + LineStyleEnum, + MarkerStyleEnum, +) + +__doc__ = """ +plotMohrCircles module provides a set of functions to plot multiple Mohr's +circles and a failure envelope from a list of MohrCircle and MohrCoulomb +objects respectively. +""" + + +def createMohrCirclesFigure( + mohrCircles: list[MohrCircle], mohrCoulomb: MohrCoulomb, userChoices: dict[str, Any] +) -> Figure: + """Create Mohr's circle figure. + + Args: + mohrCircles (list[MohrCircle]): list of MohrCircle objects. + + mohrCoulomb (MohrCoulomb): MohrCoulomb object defining the failure + envelope. + + userChoices (dict[str, Any]): dictionnary to define figure properties. + + Returns: + Figure: Figure object + """ + plt.close() + + # create figure + fig, ax = plt.subplots(constrained_layout=True) + + # plot Mohr's Circles + curvesAspect: dict[str, Any] = userChoices.get("curvesAspect", {}) + annotate: bool = userChoices.get("annotateCircles", False) + _plotMohrCircles(ax, mohrCircles, curvesAspect, annotate) + + # plot Mohr Coulomb failure envelop + failureEnvelopeAspect: dict[str, Any] = curvesAspect.get(FAILURE_ENVELOPE, {}) + _plotMohrCoulomb(ax, mohrCoulomb, failureEnvelopeAspect) + + # set user preferences + _setUserChoices(ax, userChoices) + + return fig + + +def _plotMohrCircles( + ax: Axes, + mohrCircles: list[MohrCircle], + circlesAspect: dict[str, dict[str, Any]], + annotate: bool, +) -> None: + """Plot multiple Mohr's circles on input Axes. + + Args: + ax (Axes): Axes where to plot Mohr's circles + + mohrCircles (list[MohrCircle]): list of MohrCircle objects to plot. + + circlesAspect (dict[str, dict[str, Any]]): dictionnary defining Mohr's + circle line properties. + + annotate (bool): if True, display min and max normal stress. + """ + nbPts: int = 361 + ang: npt.NDArray[np.float64] = np.linspace(0.0, np.pi, nbPts) + for mohrCircle in mohrCircles: + radius: float = mohrCircle.getCircleRadius() + xCoords = mohrCircle.getCircleCenter() + radius * np.cos(ang) + yCoords = radius * (np.sin(ang)) + label: str = mohrCircle.getCircleId() + + p: list[Line2D] # plotted lines to get the color later + if label in circlesAspect.keys(): + circleAspect: dict[str, Any] = circlesAspect[label] + color: tuple[float, float, float] = circleAspect.get("color", "k") + linestyle: str = circleAspect.get( + "linestyle", LineStyleEnum.SOLID.optionValue + ) + linewidth: float = circleAspect.get("linewidth", 1) + marker: str = circleAspect.get("marker", MarkerStyleEnum.NONE.optionValue) + markersize: float = circleAspect.get("markersize", 1) + p = ax.plot( + xCoords, + yCoords, + label=label, + color=color, + linestyle=linestyle, + linewidth=linewidth, + marker=marker, + markersize=markersize, + ) + else: + p = ax.plot(xCoords, yCoords, label=label, linestyle="-", marker="") + + if annotate: + fontColor = p[0].get_color() + annot: tuple[str, str, tuple[float, float], tuple[float, float]] = ( + mcf.findAnnotateTuples(mohrCircle) + ) + ax.annotate(annot[0], xy=annot[2], ha="left", rotation=30, color=fontColor) + ax.annotate(annot[1], xy=annot[3], ha="right", rotation=30, color=fontColor) + + +def _plotMohrCoulomb( + ax: Axes, mohrCoulomb: MohrCoulomb, curvesAspect: dict[str, Any] +) -> None: + """Plot Mohr-Coulomb failure envelope in input Axes object. + + Args: + ax (Axes): Axes where to plot the failure envelope. + + mohrCoulomb (MohrCoulomb): MohrCoulomb object to define failure envelope + parameters. + + curvesAspect (dict[str, Any]): dictionnary defining line properties of + the failure envelope. + """ + xmin, xmax = ax.get_xlim() + principalStresses, shearStress = mohrCoulomb.computeFailureEnvelop(xmax) + color: tuple[float, float, float] = curvesAspect.get("color", "k") + linestyle: str = curvesAspect.get("linestyle", LineStyleEnum.SOLID.optionValue) + linewidth: float = curvesAspect.get("linewidth", 1) + marker: str = curvesAspect.get("marker", MarkerStyleEnum.NONE.optionValue) + markersize: float = curvesAspect.get("markersize", 1) + ax.plot( + principalStresses, + shearStress, + label="Failure Envelope", + color=color, + linestyle=linestyle, + linewidth=linewidth, + marker=marker, + markersize=markersize, + ) + + +def _setUserChoices(ax: Axes, userChoices: dict[str, Any]) -> None: + """Set user preferences on input Axes. + + Args: + ax (Axes): Axes object to modify. + + userChoices (dict[str, Any]): dictionnary of user-defined properties. + """ + _updateAxis(ax, userChoices) + + # set title properties + if userChoices.get("displayTitle", False): + updateTitle(ax, userChoices) + + # set legend + if userChoices.get("displayLegend", False): + _updateLegend(ax, userChoices) + + if userChoices.get("customAxisLim", False): + _updateAxisLimits(ax, userChoices) + + +def _updateAxis(ax: Axes, userChoices: dict[str, Any]) -> None: + """Update axis ticks and labels. + + Args: + ax (Axes): axes object. + + userChoices (dict[str, Any]): user parameters. + """ + # update axis labels + xlabel: str = userChoices.get("xAxis", "Normal stress") + ylabel: str = userChoices.get("xAyAxisxis", "Shear stress") + + # get unit + unitChoice: int = userChoices.get("stressUnit", 0) + unitObj: Unit = list(Pressure)[unitChoice].value + unitLabel: str = unitObj.unitLabel + + # change displayed units + xlabel += f" ({unitLabel})" + ylabel += f" ({unitLabel})" + ax.set_xlabel(xlabel) + ax.set_ylabel(ylabel) + + # function to do conversion and set format + def _tickFormatterFunc(x: float, pos: str) -> str: + return f"{convert(x, unitObj):.2E}" + + # apply formatting to xticks and yticks + ax.xaxis.set_major_formatter(ticker.FuncFormatter(_tickFormatterFunc)) + ax.yaxis.set_major_formatter(ticker.FuncFormatter(_tickFormatterFunc)) + + # set axis properties + ax.set_aspect("equal", anchor="C") + xmin, xmax = ax.get_xlim() + ax.set_xlim(0.0) + ax.set_ylim(0.0, xmax) + ax.grid() + ax.minorticks_off() + if "minorticks" in userChoices.keys() and userChoices["minorticks"]: + ax.minorticks_on() + + +def updateTitle(ax: Axes, userChoices: dict[str, Any]) -> None: + """Update title. + + Args: + ax (Axes): axes object. + + userChoices (dict[str, Any]): user parameters. + """ + title = userChoices.get("title", "Mohr's Circles") + style = userChoices.get("titleStyle", FontStyleEnum.NORMAL.optionValue) + weight = userChoices.get("titleWeight", FontWeightEnum.BOLD.optionValue) + size = userChoices.get("titleSize", 12) + ax.set_title(title, fontstyle=style, weight=weight, fontsize=size) + + +def _updateLegend(ax: Axes, userChoices: dict[str, Any]) -> None: + """Update legend. + + Args: + ax (Axes): axes object. + + userChoices (dict[str, Any]): user parameters. + """ + loc = userChoices.get("legendPosition", LegendLocationEnum.BEST.optionValue) + size = userChoices.get("legendSize", 10) + ax.legend(loc=loc, fontsize=size) + + +def _updateAxisLimits(ax: Axes, userChoices: dict[str, Any]) -> None: + """Update axis limits. + + Args: + ax (Axes): axes object. + + userChoices (dict[str, Any]): user parameters. + """ + xmin, xmax = ax.get_xlim() + if userChoices.get("limMinX", None) is not None: + xmin = userChoices["limMinX"] + if userChoices.get("limMaxX", None) is not None: + xmax = userChoices["limMaxX"] + ax.set_xlim(xmin, xmax) + + ymin, ymax = ax.get_xlim() + if userChoices.get("limMinY", None) is not None: + ymin = userChoices["limMinY"] + if userChoices.get("limMaxY", None) is not None: + ymax = userChoices["limMaxY"] + ax.set_ylim(ymin, ymax) diff --git a/geos-posp/src/geos_posp/visu/pythonViewUtils/Figure2DGenerator.py b/geos-posp/src/geos_posp/visu/pythonViewUtils/Figure2DGenerator.py new file mode 100644 index 00000000..b585922a --- /dev/null +++ b/geos-posp/src/geos_posp/visu/pythonViewUtils/Figure2DGenerator.py @@ -0,0 +1,146 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto + +from typing import Any + +import pandas as pd # type: ignore[import-untyped] +from matplotlib import axes, figure, lines # type: ignore[import-untyped] +from matplotlib.font_manager import ( # type: ignore[import-untyped] + FontProperties, # type: ignore[import-untyped] +) +from typing_extensions import Self + +import geos_posp.visu.pythonViewUtils.functionsFigure2DGenerator as fcts +from geos_posp.utils.Logger import Logger, getLogger + + +class Figure2DGenerator: + def __init__( + self: Self, dataframe: pd.DataFrame, userChoices: dict[str, list[str]] + ) -> None: + """Utility to create cross plots using Python View. + + We want to plot f(X) = Y where in this class, + "X" will be called "variable", "Y" will be called "curves". + + Args: + dataframe (pd.DataFrame): data to plot + userChoices (dict[str, list[str]]): user choices. + """ + self.m_dataframe: pd.DataFrame = dataframe + self.m_userChoices: dict[str, Any] = userChoices + self.m_fig: figure.Figure + self.m_axes: list[axes._axes.Axes] = [] + self.m_lines: list[lines.Line2D] = [] + self.m_labels: list[str] = [] + self.m_logger: Logger = getLogger("Python View Configurator") + + try: + # apply minus 1 multiplication on certain columns + self.initMinus1Multiplication() + # defines m_fig, m_axes, m_lines and m_lables + self.plotInitialFigure() + # then to edit and customize the figure + self.enhanceFigure() + self.m_logger.info("Data were successfully plotted.") + + except Exception as e: + mess: str = "Plot creation failed due to:" + self.m_logger.critical(mess) + self.m_logger.critical(e, exc_info=True) + + def initMinus1Multiplication(self: Self) -> None: + """Multiply by -1 certain columns of the input dataframe.""" + df: pd.DataFrame = self.m_dataframe.copy(deep=True) + minus1CurveNames: list[str] = self.m_userChoices["curveConvention"] + for name in minus1CurveNames: + df[name] = df[name] * (-1) + self.m_dataframe = df + + def enhanceFigure(self: Self) -> None: + """Apply all the enhancement features to the initial figure.""" + self.changeTitle() + self.changeMinorticks() + self.changeAxisScale() + self.changeAxisLimits() + + def plotInitialFigure(self: Self) -> None: + """Generates a figure and axes objects from matplotlib. + + The figure plots all the curves along the X or Y axis, with legend and + label for X and Y. + """ + if self.m_userChoices["plotRegions"]: + if not self.m_userChoices["reverseXY"]: + (fig, ax_all, lines, labels) = fcts.multipleSubplots( + self.m_dataframe, self.m_userChoices + ) + else: + (fig, ax_all, lines, labels) = fcts.multipleSubplotsInverted( + self.m_dataframe, self.m_userChoices + ) + else: + if not self.m_userChoices["reverseXY"]: + (fig, ax_all, lines, labels) = fcts.oneSubplot( + self.m_dataframe, self.m_userChoices + ) + else: + (fig, ax_all, lines, labels) = fcts.oneSubplotInverted( + self.m_dataframe, self.m_userChoices + ) + self.m_fig = fig + self.m_axes = ax_all + self.m_lines = lines + self.m_labels = labels + + def changeTitle(self: Self) -> None: + """Update title of the first axis of the figure based on user choices.""" + if self.m_userChoices["displayTitle"]: + title: str = self.m_userChoices["title"] + fontTitle: FontProperties = fcts.buildFontTitle(self.m_userChoices) + self.m_fig.suptitle(title, fontproperties=fontTitle) + + def changeMinorticks(self: Self) -> None: + """Set the minorticks on or off for every axes.""" + choice: bool = self.m_userChoices["minorticks"] + if choice: + for ax in self.m_axes: + ax.minorticks_on() + else: + for ax in self.m_axes: + ax.minorticks_off() + + def changeAxisScale(self: Self) -> None: + """Set the minorticks on or off for every axes.""" + for ax in self.m_axes: + if self.m_userChoices["logScaleX"]: + ax.set_xscale("log") + if self.m_userChoices["logScaleY"]: + ax.set_yscale("log") + + def changeAxisLimits(self: Self) -> None: + """Update axis limits.""" + if self.m_userChoices["customAxisLim"]: + for ax in self.m_axes: + xmin, xmax = ax.get_xlim() + if self.m_userChoices["limMinX"] is not None: + xmin = self.m_userChoices["limMinX"] + if self.m_userChoices["limMaxX"] is not None: + xmax = self.m_userChoices["limMaxX"] + ax.set_xlim(xmin, xmax) + + ymin, ymax = ax.get_ylim() + if self.m_userChoices["limMinY"] is not None: + ymin = self.m_userChoices["limMinY"] + if self.m_userChoices["limMaxY"] is not None: + ymax = self.m_userChoices["limMaxY"] + ax.set_ylim(ymin, ymax) + + def getFigure(self: Self) -> figure.Figure: + """Acces the m_fig attribute. + + Returns: + figure.Figure: Figure containing all the plots. + """ + return self.m_fig diff --git a/geos-posp/src/geos_posp/visu/pythonViewUtils/__init__.py b/geos-posp/src/geos_posp/visu/pythonViewUtils/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/src/geos_posp/visu/pythonViewUtils/functionsFigure2DGenerator.py b/geos-posp/src/geos_posp/visu/pythonViewUtils/functionsFigure2DGenerator.py new file mode 100644 index 00000000..6547adfe --- /dev/null +++ b/geos-posp/src/geos_posp/visu/pythonViewUtils/functionsFigure2DGenerator.py @@ -0,0 +1,1424 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +import math +from typing import Any + +import matplotlib.pyplot as plt # type: ignore[import-untyped] +import numpy as np +import numpy.typing as npt +import pandas as pd # type: ignore[import-untyped] +from matplotlib import axes, figure, lines # type: ignore[import-untyped] +from matplotlib.font_manager import ( # type: ignore[import-untyped] + FontProperties, # type: ignore[import-untyped] +) + +import geos_posp.processing.geosLogReaderFunctions as fcts + +""" +Plotting tools for 2D figure and axes generation. +""" + + +def oneSubplot( + df: pd.DataFrame, userChoices: dict[str, Any] +) -> tuple[figure.Figure, list[axes.Axes], list[lines.Line2D], list[str]]: + """Created a single subplot. + + From a dataframe, knowing which curves to plot along which variable, + generates a fig and its list of axes with the data plotted. + + Args: + df (pd.DataFrame): dataframe containing at least two columns, + one named "variableName" and the other "curveName" + userChoices (dict[str, Any]): Choices made by widget selection + in PythonViewConfigurator filter. + + Returns: + tuple[figure.Figure, list[axes.Axes], + list[lines.Line2D] , list[str]]: the fig and its list of axes. + """ + curveNames: list[str] = userChoices["curveNames"] + variableName: str = userChoices["variableName"] + curvesAspect: dict[ + str, tuple[tuple[float, float, float], str, float, str, float] + ] = userChoices["curvesAspect"] + associatedProperties: dict[str, list[str]] = associatePropertyToAxeType(curveNames) + fig, ax = plt.subplots(constrained_layout=True) + all_ax: list[axes.Axes] = setupAllAxes(ax, variableName, associatedProperties, True) + lineList: list[lines.Line2D] = [] + labels: list[str] = [] + cpt_cmap: int = 0 + x: npt.NDArray[np.float64] = df[variableName].to_numpy() + for cpt_ax, (ax_name, propertyNames) in enumerate(associatedProperties.items()): + ax_to_use: axes.Axes = setupAxeToUse(all_ax, cpt_ax, ax_name, False) + for propName in propertyNames: + y: npt.NDArray[np.float64] = df[propName].to_numpy() + plotAxe(ax_to_use, x, y, propName, cpt_cmap, curvesAspect) + cpt_cmap += 1 + new_lines, new_labels = ax_to_use.get_legend_handles_labels() + lineList += new_lines # type: ignore[arg-type] + labels += new_labels + labels, lineList = smartLabelsSorted(labels, lineList, userChoices) + if userChoices["displayLegend"]: + ax.legend( + lineList, + labels, + loc=userChoices["legendPosition"], + fontsize=userChoices["legendSize"], + ) + ax.grid() + return (fig, all_ax, lineList, labels) + + +def oneSubplotInverted( + df: pd.DataFrame, userChoices: dict[str, Any] +) -> tuple[figure.Figure, list[axes.Axes], list[lines.Line2D], list[str]]: + """Created a single subplot with inverted X Y axes. + + From a dataframe, knowing which curves to plot along which variable, + generates a fig and its list of axes with the data plotted. + + Args: + df (pd.DataFrame): dataframe containing at least two columns, + one named "variableName" and the other "curveName" + userChoices (dict[str, Any]): Choices made by widget selection + in PythonViewConfigurator filter. + + Returns: + tuple[figure.Figure, list[axes.Axes], + list[lines.Line2D] , list[str]]: the fig and its list of axes. + """ + curveNames: list[str] = userChoices["curveNames"] + variableName: str = userChoices["variableName"] + curvesAspect: dict[ + str, tuple[tuple[float, float, float], str, float, str, float] + ] = userChoices["curvesAspect"] + associatedProperties: dict[str, list[str]] = associatePropertyToAxeType(curveNames) + fig, ax = plt.subplots(constrained_layout=True) + all_ax: list[axes.Axes] = setupAllAxes( + ax, variableName, associatedProperties, False + ) + linesList: list[lines.Line2D] = [] + labels: list[str] = [] + cpt_cmap: int = 0 + y: npt.NDArray[np.float64] = df[variableName].to_numpy() + for cpt_ax, (ax_name, propertyNames) in enumerate(associatedProperties.items()): + ax_to_use: axes.Axes = setupAxeToUse(all_ax, cpt_ax, ax_name, True) + for propName in propertyNames: + x: npt.NDArray[np.float64] = df[propName].to_numpy() + plotAxe(ax_to_use, x, y, propName, cpt_cmap, curvesAspect) + cpt_cmap += 1 + new_lines, new_labels = ax_to_use.get_legend_handles_labels() + linesList += new_lines # type: ignore[arg-type] + labels += new_labels + labels, linesList = smartLabelsSorted(labels, linesList, userChoices) + if userChoices["displayLegend"]: + ax.legend( + linesList, + labels, + loc=userChoices["legendPosition"], + fontsize=userChoices["legendSize"], + ) + ax.grid() + return (fig, all_ax, linesList, labels) + + +def multipleSubplots( + df: pd.DataFrame, userChoices: dict[str, Any] +) -> tuple[figure.Figure, list[axes.Axes], list[lines.Line2D], list[str]]: + """Created multiple subplots. + + From a dataframe, knowing which curves to plot along which variable, + generates a fig and its list of axes with the data plotted. + + Args: + df (pd.DataFrame): dataframe containing at least two columns, + one named "variableName" and the other "curveName". + userChoices (dict[str, Any]): Choices made by widget selection + in PythonViewConfigurator filter. + + Returns: + tuple[figure.Figure, list[axes.Axes], + list[lines.Line2D] , list[str]]: the fig and its list of axes. + """ + curveNames: list[str] = userChoices["curveNames"] + variableName: str = userChoices["variableName"] + curvesAspect: dict[ + str, tuple[tuple[float, float, float], str, float, str, float] + ] = userChoices["curvesAspect"] + ratio: float = userChoices["ratio"] + assosIdentifiers: dict[str, dict[str, list[str]]] = associationIdentifiers( + curveNames + ) + nbr_suplots: int = len(assosIdentifiers.keys()) + # if only one subplots needs to be created + if nbr_suplots == 1: + return oneSubplot(df, userChoices) + + layout: tuple[int, int, int] = smartLayout(nbr_suplots, ratio) + fig, axs0 = plt.subplots(layout[0], layout[1], constrained_layout=True) + axs: list[axes.Axes] = axs0.flatten().tolist() # type: ignore[union-attr] + for i in range(layout[2]): + fig.delaxes(axs[-(i + 1)]) + all_lines: list[lines.Line2D] = [] + all_labels: list[str] = [] + # first loop for subplots + propertiesExtremas: dict[str, tuple[float, float]] = ( + findExtremasPropertiesForAssociatedIdentifiers(df, assosIdentifiers, True) + ) + for j, identifier in enumerate(assosIdentifiers.keys()): + first_ax: axes.Axes = axs[j] + associatedProperties: dict[str, list[str]] = assosIdentifiers[identifier] + all_ax: list[axes.Axes] = setupAllAxes( + first_ax, variableName, associatedProperties, True + ) + axs += all_ax[1:] + linesList: list[lines.Line2D] = [] + labels: list[str] = [] + cpt_cmap: int = 0 + x: npt.NDArray[np.float64] = df[variableName].to_numpy() + # second loop for axes per subplot + for cpt_ax, (ax_name, propertyNames) in enumerate(associatedProperties.items()): + ax_to_use: axes.Axes = setupAxeToUse(all_ax, cpt_ax, ax_name, False) + for propName in propertyNames: + y: npt.NDArray[np.float64] = df[propName].to_numpy() + plotAxe(ax_to_use, x, y, propName, cpt_cmap, curvesAspect) + ax_to_use.set_ylim(*propertiesExtremas[ax_name]) + cpt_cmap += 1 + new_lines, new_labels = ax_to_use.get_legend_handles_labels() + linesList += new_lines # type: ignore[arg-type] + all_lines += new_lines # type: ignore[arg-type] + labels += new_labels + all_labels += new_labels + labels, linesList = smartLabelsSorted(labels, linesList, userChoices) + if userChoices["displayLegend"]: + first_ax.legend( + linesList, + labels, + loc=userChoices["legendPosition"], + fontsize=userChoices["legendSize"], + ) + if userChoices["displayTitle"]: + first_ax.set_title(identifier, fontsize=10) + first_ax.grid() + return (fig, axs, all_lines, all_labels) + + +def multipleSubplotsInverted( + df: pd.DataFrame, userChoices: dict[str, Any] +) -> tuple[figure.Figure, list[axes.Axes], list[lines.Line2D], list[str]]: + """Created multiple subplots with inverted X Y axes. + + From a dataframe, knowing which curves to plot along which variable, + generates a fig and its list of axes with the data plotted. + + Args: + df (pd.DataFrame): dataframe containing at least two columns, + one named "variableName" and the other "curveName". + userChoices (dict[str, Any]): Choices made by widget selection + in PythonViewConfigurator filter. + + Returns: + tuple[figure.Figure, list[axes.Axes], + list[lines.Line2D] , list[str]]: the fig and its list of axes. + """ + curveNames: list[str] = userChoices["curveNames"] + variableName: str = userChoices["variableName"] + curvesAspect: dict[ + str, tuple[tuple[float, float, float], str, float, str, float] + ] = userChoices["curvesAspect"] + ratio: float = userChoices["ratio"] + assosIdentifiers: dict[str, dict[str, list[str]]] = associationIdentifiers( + curveNames + ) + nbr_suplots: int = len(assosIdentifiers.keys()) + # if only one subplots needs to be created + if nbr_suplots == 1: + return oneSubplotInverted(df, userChoices) + + layout: tuple[int, int, int] = smartLayout(nbr_suplots, ratio) + fig, axs0 = plt.subplots(layout[0], layout[1], constrained_layout=True) + axs: list[axes.Axes] = axs0.flatten().tolist() # type: ignore[union-attr] + for i in range(layout[2]): + fig.delaxes(axs[-(i + 1)]) + all_lines: list[lines.Line2D] = [] + all_labels: list[str] = [] + # first loop for subplots + propertiesExtremas: dict[str, tuple[float, float]] = ( + findExtremasPropertiesForAssociatedIdentifiers(df, assosIdentifiers, True) + ) + for j, identifier in enumerate(assosIdentifiers.keys()): + first_ax: axes.Axes = axs[j] + associatedProperties: dict[str, list[str]] = assosIdentifiers[identifier] + all_ax: list[axes.Axes] = setupAllAxes( + first_ax, variableName, associatedProperties, False + ) + axs += all_ax[1:] + linesList: list[lines.Line2D] = [] + labels: list[str] = [] + cpt_cmap: int = 0 + y: npt.NDArray[np.float64] = df[variableName].to_numpy() + # second loop for axes per subplot + for cpt_ax, (ax_name, propertyNames) in enumerate(associatedProperties.items()): + ax_to_use: axes.Axes = setupAxeToUse(all_ax, cpt_ax, ax_name, True) + for propName in propertyNames: + x: npt.NDArray[np.float64] = df[propName].to_numpy() + plotAxe(ax_to_use, x, y, propName, cpt_cmap, curvesAspect) + ax_to_use.set_xlim(propertiesExtremas[ax_name]) + cpt_cmap += 1 + new_lines, new_labels = ax_to_use.get_legend_handles_labels() + linesList += new_lines # type: ignore[arg-type] + all_lines += new_lines # type: ignore[arg-type] + labels += new_labels + all_labels += new_labels + labels, linesList = smartLabelsSorted(labels, linesList, userChoices) + if userChoices["displayLegend"]: + first_ax.legend( + linesList, + labels, + loc=userChoices["legendPosition"], + fontsize=userChoices["legendSize"], + ) + if userChoices["displayTitle"]: + first_ax.set_title(identifier, fontsize=10) + first_ax.grid() + return (fig, axs, all_lines, all_labels) + + +def setupAllAxes( + first_ax: axes.Axes, + variableName: str, + associatedProperties: dict[str, list[str]], + axisX: bool, +) -> list[axes.Axes]: + """Modify axis name and ticks avec X or Y axis of all subplots. + + Args: + first_ax (axes.Axes): subplot id. + variableName (str): name of the axis. + associatedProperties (dict[str, list[str]]): Name of the properties + axisX (bool): X (True) or Y (False) axis to modify. + + Returns: + list[axes.Axes]: modified subplots + """ + all_ax: list[axes.Axes] = [first_ax] + if axisX: + first_ax.set_xlabel(variableName) + first_ax.ticklabel_format( + style="sci", axis="x", scilimits=(0, 0), useMathText=True + ) + for i in range(1, len(associatedProperties.keys())): + second_ax = first_ax.twinx() + assert isinstance(second_ax, axes.Axes) + all_ax.append(second_ax) + all_ax[i].spines["right"].set_position(("axes", 1 + 0.07 * (i - 1))) + all_ax[i].tick_params(axis="y", which="both", left=False, right=True) + all_ax[i].yaxis.set_ticks_position("right") + all_ax[i].yaxis.offsetText.set_position((1.04 + 0.07 * (i - 1), 0)) + first_ax.yaxis.offsetText.set_position((-0.04, 0)) + else: + first_ax.set_ylabel(variableName) + first_ax.ticklabel_format( + style="sci", axis="y", scilimits=(0, 0), useMathText=True + ) + for i in range(1, len(associatedProperties.keys())): + second_ax = first_ax.twiny() + assert isinstance(second_ax, axes.Axes) + all_ax.append(second_ax) + all_ax[i].spines["bottom"].set_position(("axes", -0.08 * i)) + all_ax[i].xaxis.set_label_position("bottom") + all_ax[i].tick_params(axis="x", which="both", bottom=True, top=False) + all_ax[i].xaxis.set_ticks_position("bottom") + return all_ax + + +def setupAxeToUse( + all_ax: list[axes.Axes], axeId: int, ax_name: str, axisX: bool +) -> axes.Axes: + """Modify axis name and ticks avec X or Y axis of subplot axeId in all_ax. + + Args: + all_ax (list[axes.Axes]): list of all subplots + axeId (int): id of the subplot + ax_name (str): name of the X or Y axis + axisX (bool): X (True) or Y (False) axis to modify. + + Returns: + axes.Axes: modified subplot + """ + ax_to_use: axes.Axes = all_ax[axeId] + if axisX: + ax_to_use.set_xlabel(ax_name) + ax_to_use.ticklabel_format( + style="sci", axis="x", scilimits=(0, 0), useMathText=True + ) + else: + ax_to_use.set_ylabel(ax_name) + ax_to_use.ticklabel_format( + style="sci", axis="y", scilimits=(0, 0), useMathText=True + ) + return ax_to_use + + +def plotAxe( + ax_to_use: axes.Axes, + x: npt.NDArray[np.float64], + y: npt.NDArray[np.float64], + propertyName: str, + cpt_cmap: int, + curvesAspect: dict[str, tuple[tuple[float, float, float], str, float, str, float]], +) -> None: + """Plot x, y data using input ax_to_use according to curvesAspect. + + Args: + ax_to_use (axes.Axes): subplot to use + x (npt.NDArray[np.float64]): abscissa data + y (npt.NDArray[np.float64]): ordinate data + propertyName (str): name of the property + cpt_cmap (int): colormap to use + curvesAspect (dict[str, tuple[tuple[float, float, float],str, float, str, float]]): + user choices on curve aspect + """ + cmap = plt.rcParams["axes.prop_cycle"].by_key()["color"][cpt_cmap % 10] + mask = np.logical_and(np.isnan(x), np.isnan(y)) + not_mask = ~mask + # Plot only when x and y values are not nan values + if propertyName in curvesAspect: + asp: tuple[tuple[float, float, float], str, float, str, float] = curvesAspect[ + propertyName + ] + ax_to_use.plot( + x[not_mask], + y[not_mask], + label=propertyName, + color=asp[0], + linestyle=asp[1], + linewidth=asp[2], + marker=asp[3], + markersize=asp[4], + ) + else: + ax_to_use.plot(x[not_mask], y[not_mask], label=propertyName, color=cmap) + + +def getExtremaAllAxes( + axes: list[axes.Axes], +) -> tuple[tuple[float, float], tuple[float, float]]: + """Gets the limits of both X and Y axis as a 2x2 element tuple. + + Args: + axes (list[axes.Axes]): list of subplots to get limits. + + Returns: + tuple[tuple[float, float], tuple[float, float]]:: ((xMin, xMax), (yMin, yMax)) + """ + assert len(axes) > 0 + xMin, xMax, yMin, yMax = getAxeLimits(axes[0]) + if len(axes) > 1: + for i in range(1, len(axes)): + x1, x2, y1, y2 = getAxeLimits(axes[i]) + if x1 < xMin: + xMin = x1 + if x2 > xMax: + xMax = x2 + if y1 < yMin: + yMin = y1 + if y2 > yMax: + yMax = y2 + return ((xMin, xMax), (yMin, yMax)) + + +def getAxeLimits(ax: axes.Axes) -> tuple[float, float, float, float]: + """Gets the limits of both X and Y axis as a 4 element tuple. + + Args: + ax (axes.Axes): subplot to get limits. + + Returns: + tuple[float, float, float, float]: (xMin, xMax, yMin, yMax) + """ + xMin, xMax = ax.get_xlim() + yMin, yMax = ax.get_ylim() + return (xMin, xMax, yMin, yMax) + + +def findExtremasPropertiesForAssociatedIdentifiers( + df: pd.DataFrame, + associatedIdentifiers: dict[str, dict[str, list[str]]], + offsetPlotting: bool = False, + offsetPercentage: int = 5, +) -> dict[str, tuple[float, float]]: + """Find min and max of all properties linked to a same identifier. + + Using an associatedIdentifiers dict containing associatedProperties dict, + we can find the extremas for each property of each identifier. Once we have them all, + we compare for each identifier what are the most extreme values and only the biggest and + lowest are kept in the end. + + + Args: + df (pd.DataFrame): Pandas dataframe + associatedIdentifiers (dict[str, dict[str, list[str]]]): property identifiers. + offsetPlotting (bool, optional): When using the values being returned, + we might want to add an offset to these values. If set to True, + the offsetPercentage is taken into account. Defaults to False. + offsetPercentage (int, optional): Value by which we will offset + the min and max values of each tuple of floats. Defaults to 5. + + Returns: + dict[str, tuple[float, float]]: { + "BHP (Pa)": (minAllWells, maxAllWells), + "TotalMassRate (kg)": (minAllWells, maxAllWells), + "TotalSurfaceVolumetricRate (m3/s)": (minAllWells, maxAllWells), + "SurfaceVolumetricRateCO2 (m3/s)": (minAllWells, maxAllWells), + "SurfaceVolumetricRateWater (m3/s)": (minAllWells, maxAllWells) + } + """ + extremasProperties: dict[str, tuple[float, float]] = {} + # first we need to find the extrema for each property type per region + propertyTypesExtremas: dict[str, list[tuple[float, float]]] = {} + for associatedProperties in associatedIdentifiers.values(): + extremasPerProperty: dict[str, tuple[float, float]] = ( + findExtremasAssociatedProperties(df, associatedProperties) + ) + for propertyType, extremaFound in extremasPerProperty.items(): + if propertyType not in propertyTypesExtremas: + propertyTypesExtremas[propertyType] = [extremaFound] + else: + propertyTypesExtremas[propertyType].append(extremaFound) + # then, once all extrema have been found for all regions, we need to figure out + # which extrema per property type is the most extreme one + for propertyType in propertyTypesExtremas: + values: list[tuple[float, float]] = propertyTypesExtremas[propertyType] + minValues: list[float] = [values[i][0] for i in range(len(values))] + maxValues: list[float] = [values[i][1] for i in range(len(values))] + lowest, highest = (min(minValues), max(maxValues)) + if offsetPlotting: + offset: float = (highest - lowest) / 100 * offsetPercentage + lowest, highest = (lowest - offset, highest + offset) + extremasProperties[propertyType] = (lowest, highest) + return extremasProperties + + +def findExtremasAssociatedProperties( + df: pd.DataFrame, associatedProperties: dict[str, list[str]] +) -> dict[str, tuple[float, float]]: + """Find the min and max of properties. + + Using an associatedProperties dict containing property types + as keys and a list of property names as values, + and a pandas dataframe whose column names are composed of those same + property names, you can find the min and max values of each property + type and return it as a tuple. + + Args: + df (pd.DataFrame): Pandas dataframe + associatedProperties (dict[str, list[str]]): { + "Pressure (Pa)": ["Reservoir__Pressure__Pa__Source1"], + "Mass (kg)": ["CO2__Mass__kg__Source1", + "Water__Mass__kg__Source1"] + } + + Returns: + dict[str, tuple[float, float]]: { + "Pressure (Pa)": (minPressure, maxPressure), + "Mass (kg)": (minMass, maxMass) + } + """ + extremasProperties: dict[str, tuple[float, float]] = {} + for propertyType, propertyNames in associatedProperties.items(): + minValues = np.empty(len(propertyNames)) + maxValues = np.empty(len(propertyNames)) + for i, propertyName in enumerate(propertyNames): + values: npt.NDArray[np.float64] = df[propertyName].to_numpy() + minValues[i] = np.nanmin(values) + maxValues[i] = np.nanmax(values) + extrema: tuple[float, float] = ( + float(np.min(minValues)), + float(np.max(maxValues)), + ) + extremasProperties[propertyType] = extrema + return extremasProperties + + +""" +Utils for treatment of the data +""" + + +def associatePropertyToAxeType(propertyNames: list[str]) -> dict[str, list[str]]: + """Identify property types. + + From a list of property names, identify if each of this property + corresponds to a certain property type like "Pressure", "Mass", + "Temperature" etc ... and returns a dict where the keys are the property + type and the value the list of property names associated to it. + + Args: + propertyNames (list[str]): ["Reservoir__Pressure__Pa__Source1", + "CO2__Mass__kg__Source1", "Water__Mass__kg__Source1"] + + Returns: + dict[str, list[str]]: { "Pressure (Pa)": ["Reservoir__Pressure__Pa__Source1"], + "Mass (kg)": ["CO2__Mass__kg__Source1", + "Water__Mass__kg__Source1"] } + """ + propertyIds: list[str] = fcts.identifyProperties(propertyNames) + associationTable: dict[str, str] = { + "0": "Pressure", + "1": "Pressure", + "2": "Temperature", + "3": "PoreVolume", + "4": "PoreVolume", + "5": "Mass", + "6": "Mass", + "7": "Mass", + "8": "Mass", + "9": "Mass", + "10": "Mass", + "11": "BHP", + "12": "MassRate", + "13": "VolumetricRate", + "14": "VolumetricRate", + "15": "BHP", + "16": "MassRate", + "17": "VolumetricRate", + "18": "VolumetricRate", + "19": "VolumetricRate", + "20": "Volume", + "21": "VolumetricRate", + "22": "Volume", + "23": "Iterations", + "24": "Iterations", + "25": "Stress", + "26": "Displacement", + "27": "Permeability", + "28": "Porosity", + "29": "Ratio", + "30": "Fraction", + "31": "BulkModulus", + "32": "ShearModulus", + "33": "OedometricModulus", + "34": "Points", + "35": "Density", + "36": "Mass", + "37": "Mass", + "38": "Time", + "39": "Time", + } + associatedPropertyToAxeType: dict[str, list[str]] = {} + noUnitProperties: list[str] = [ + "Iterations", + "Porosity", + "Ratio", + "Fraction", + "OedometricModulus", + ] + for i, propId in enumerate(propertyIds): + idProp: str = propId.split(":")[0] + propNoId: str = propId.split(":")[1] + associatedType: str = associationTable[idProp] + if associatedType in noUnitProperties: + axeName: str = associatedType + else: + propIdElts: list[str] = propNoId.split("__") + # no unit was found + if len(propIdElts) <= 2: + axeName = associatedType + # there is a unit + else: + unit: str = propIdElts[-2] + axeName = associatedType + " (" + unit + ")" + if axeName not in associatedPropertyToAxeType: + associatedPropertyToAxeType[axeName] = [] + associatedPropertyToAxeType[axeName].append(propertyNames[i]) + return associatedPropertyToAxeType + + +def propertiesPerIdentifier(propertyNames: list[str]) -> dict[str, list[str]]: + """Extract identifiers with associatied properties. + + From a list of property names, extracts the identifier (name of the + region for flow property or name of a well for well property) and creates + a dictionnary with identifiers as keys and the properties containing them + for value in a list. + + Args: + propertyNames (list[str]): property names + Example + + .. code-block:: python + + [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1", + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1" + ] + + Returns: + dict[str, list[str]]: property identifiers + Example + + .. code-block:: python + + { + "WellControls1": [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1" + ], + "WellControls2": [ + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1" + ] + } + """ + propsPerIdentfier: dict[str, list[str]] = {} + for propertyName in propertyNames: + elements: list[str] = propertyName.split("__") + identifier: str = elements[0] + if identifier not in propsPerIdentfier: + propsPerIdentfier[identifier] = [] + propsPerIdentfier[identifier].append(propertyName) + return propsPerIdentfier + + +def associationIdentifiers(propertyNames: list[str]) -> dict[str, dict[str, list[str]]]: + """Extract identifiers with associatied curves. + + From a list of property names, extracts the identifier (name of the + region for flow property or name of a well for well property) and creates + a dictionnary with identifiers as keys and the properties containing them + for value in a list. + + Args: + propertyNames (list[str]): property names + Example + + .. code-block:: python + + [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1", + "WellControls1__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1", + "WellControls2__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls3__BHP__Pa__Source1", + "WellControls3__TotalMassRate__tons/day__Source1", + "WellControls3__TotalSurfaceVolumetricRate__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateCO2__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateWater__bbl/day__Source1", + "Mean__BHP__Pa__Source1", + "Mean__TotalMassRate__tons/day__Source1", + "Mean__TotalSurfaceVolumetricRate__bbl/day__Source1", + "Mean__SurfaceVolumetricRateCO2__bbl/day__Source1", + "Mean__SurfaceVolumetricRateWater__bbl/day__Source1" + ] + + Returns: + dict[str, dict[str, list[str]]]: property identifiers + Example + + .. code-block:: python + + { + "WellControls1": { + 'BHP (Pa)': [ + 'WellControls1__BHP__Pa__Source1' + ], + 'MassRate (kg/s)': [ + 'WellControls1__TotalMassRate__kg/s__Source1' + ], + 'VolumetricRate (m3/s)': [ + 'WellControls1__TotalSurfaceVolumetricRate__m3/s__Source1', + 'WellControls1__SurfaceVolumetricRateCO2__m3/s__Source1', + 'WellControls1__SurfaceVolumetricRateWater__m3/s__Source1' + ] + }, + "WellControls2": { + 'BHP (Pa)': [ + 'WellControls2__BHP__Pa__Source1' + ], + 'MassRate (kg/s)': [ + 'WellControls2__TotalMassRate__kg/s__Source1' + ], + 'VolumetricRate (m3/s)': [ + 'WellControls2__TotalSurfaceVolumetricRate__m3/s__Source1', + 'WellControls2__SurfaceVolumetricRateCO2__m3/s__Source1', + 'WellControls2__SurfaceVolumetricRateWater__m3/s__Source1' + ] + }, + "WellControls3": { + 'BHP (Pa)': [ + 'WellControls3__BHP__Pa__Source1' + ], + 'MassRate (tons/day)': [ + 'WellControls3__TotalMassRate__tons/day__Source1' + ], + 'VolumetricRate (bbl/day)': [ + 'WellControls3__TotalSurfaceVolumetricRate__bbl/day__Source1', + 'WellControls3__SurfaceVolumetricRateCO2__bbl/day__Source1', + 'WellControls3__SurfaceVolumetricRateWater__bbl/day__Source1' + ] + }, + "Mean": { + 'BHP (Pa)': [ + 'Mean__BHP__Pa__Source1' + ], + 'MassRate (tons/day)': [ + 'Mean__TotalMassRate__tons/day__Source1' + ], + 'VolumetricRate (bbl/day)': [ + 'Mean__TotalSurfaceVolumetricRate__bbl/day__Source1', + 'Mean__SurfaceVolumetricRateCO2__bbl/day__Source1', + 'Mean__SurfaceVolumetricRateWater__bbl/day__Source1' + ] + } + } + """ + propsPerIdentfier: dict[str, list[str]] = propertiesPerIdentifier(propertyNames) + assosIdentifier: dict[str, dict[str, list[str]]] = {} + for ident, propNames in propsPerIdentfier.items(): + assosPropsToAxeType: dict[str, list[str]] = associatePropertyToAxeType( + propNames + ) + assosIdentifier[ident] = assosPropsToAxeType + return assosIdentifier + + +def buildFontTitle(userChoices: dict[str, Any]) -> FontProperties: + """Builds a Fontproperties object according to user choices on title. + + Args: + userChoices (dict[str, Any]): customization parameters. + + Returns: + FontProperties: FontProperties object for the title. + """ + fontTitle: FontProperties = FontProperties() + if "titleStyle" in userChoices: + fontTitle.set_style(userChoices["titleStyle"]) + if "titleWeight" in userChoices: + fontTitle.set_weight(userChoices["titleWeight"]) + if "titleSize" in userChoices: + fontTitle.set_size(userChoices["titleSize"]) + return fontTitle + + +def buildFontVariable(userChoices: dict[str, Any]) -> FontProperties: + """Builds a Fontproperties object according to user choices on variables. + + Args: + userChoices (dict[str, Any]): customization parameters. + + Returns: + FontProperties: FontProperties object for the variable axes. + """ + fontVariable: FontProperties = FontProperties() + if "variableStyle" in userChoices: + fontVariable.set_style(userChoices["variableStyle"]) + if "variableWeight" in userChoices: + fontVariable.set_weight(userChoices["variableWeight"]) + if "variableSize" in userChoices: + fontVariable.set_size(userChoices["variableSize"]) + return fontVariable + + +def buildFontCurves(userChoices: dict[str, Any]) -> FontProperties: + """Builds a Fontproperties object according to user choices on curves. + + Args: + userChoices (dict[str, str]): customization parameters. + + Returns: + FontProperties: FontProperties object for the curves axes. + """ + fontCurves: FontProperties = FontProperties() + if "curvesStyle" in userChoices: + fontCurves.set_style(userChoices["curvesStyle"]) + if "curvesWeight" in userChoices: + fontCurves.set_weight(userChoices["curvesWeight"]) + if "curvesSize" in userChoices: + fontCurves.set_size(userChoices["curvesSize"]) + return fontCurves + + +def customizeLines( + userChoices: dict[str, Any], labels: list[str], linesList: list[lines.Line2D] +) -> list[lines.Line2D]: + """Customize lines according to user choices. + + By applying the user choices, we modify or not the list of lines + and return it with the same number of lines in the same order. + + Args: + userChoices (dict[str, Any]): customization parameters. + labels (list[str]): labels of lines. + linesList (list[lines.Line2D]): list of lines object. + + Returns: + list[lines.Line2D]: list of lines object modified. + """ + if "linesModified" in userChoices: + linesModifs: dict[str, dict[str, Any]] = userChoices["linesModified"] + linesChanged: list[lines.Line2D] = [] + for i, label in enumerate(labels): + if label in linesModifs: + lineChanged: lines.Line2D = applyCustomizationOnLine( + linesList[i], linesModifs[label] + ) + linesChanged.append(lineChanged) + else: + linesChanged.append(linesList[i]) + return linesChanged + else: + return linesList + + +def applyCustomizationOnLine( + line: lines.Line2D, parameters: dict[str, Any] +) -> lines.Line2D: + """Apply modification methods on a line from parameters. + + Args: + line (lines.Line2D): Matplotlib Line2D + parameters (dict[str, Any]): dictionary of { + "linestyle": one of ["-","--","-.",":"] + "linewidth": positive int + "color": color code + "marker": one of ["",".","o","^","s","*","D","+","x"] + "markersize":positive int + } + + Returns: + lines.Line2D: Line2D object modified. + """ + if "linestyle" in parameters: + line.set_linestyle(parameters["linestyle"]) + if "linewidth" in parameters: + line.set_linewidth(parameters["linewidth"]) + if "color" in parameters: + line.set_color(parameters["color"]) + if "marker" in parameters: + line.set_marker(parameters["marker"]) + if "markersize" in parameters: + line.set_markersize(parameters["markersize"]) + return line + + +""" +Layout tools for layering subplots in a figure +""" + + +def isprime(x: int) -> bool: + """Checks if a number is primer or not. + + Args: + x (int): Positive number to test. + + Returns: + bool: True if prime, False if not. + """ + if x < 0: + print("Invalid number entry, needs to be positive int") + return False + + return all(x % n != 0 for n in range(2, int(x**0.5) + 1)) + + +def findClosestPairIntegers(x: int) -> tuple[int, int]: + """Get the pair of integers that multiply the closest to input value. + + Finds the closest pair of integers that when multiplied together, + gives a number the closest to the input number (always above or equal). + + Args: + x (int): Positive number. + + Returns: + tuple[int, int]: (highest int, lowest int) + """ + if x < 4: + return (x, 1) + while isprime(x): + x += 1 + N: int = round(math.sqrt(x)) + while x > N: + if x % N == 0: + M = x // N + highest = max(M, N) + lowest = min(M, N) + return (highest, lowest) + else: + N += 1 + return (x, 1) + + +def smartLayout(x: int, ratio: float) -> tuple[int, int, int]: + """Return the best layout according to the number of subplots. + + For multiple subplots, we need to have a layout that can adapt to + the number of subplots automatically. This function figures out the + best layout possible knowing the number of suplots and the figure ratio. + + Args: + x (int): Positive number. + ratio (float): width to height ratio of a figure. + + Returns: + tuple[int]: (nbr_rows, nbr_columns, number of axes to remove) + """ + pair: tuple[int, int] = findClosestPairIntegers(x) + nbrAxesToRemove: int = pair[0] * pair[1] - x + if ratio < 1: + return (pair[0], pair[1], nbrAxesToRemove) + else: + return (pair[1], pair[0], nbrAxesToRemove) + + +""" +Legend tools +""" + +commonAssociations: dict[str, str] = { + "pressuremin": "Pmin", + "pressureMax": "Pmax", + "pressureaverage": "Pavg", + "deltapressuremin": "DPmin", + "deltapressuremax": "DPmax", + "temperaturemin": "Tmin", + "temperaturemax": "Tmax", + "temperatureaverage": "Tavg", + "effectivestressxx": "ESxx", + "effectivestresszz": "ESzz", + "effectivestressratio": "ESratio", + "totaldisplacementx": "TDx", + "totaldisplacementy": "TDy", + "totaldisplacementz": "TDz", + "totalstressXX": "TSxx", + "totalstressZZ": "TSzz", + "stressxx": "Sxx", + "stressyy": "Syy", + "stresszz": "Szz", + "stressxy": "Sxy", + "stressxz": "Sxz", + "stressyz": "Syz", + "poissonratio": "PR", + "porosity": "PORO", + "specificgravity": "SG", + "theoreticalverticalstress": "TVS", + "density": "DNST", + "pressure": "P", + "permeabilityx": "PERMX", + "permeabilityy": "PERMY", + "permeabilityz": "PERMZ", + "oedometric": "OEDO", + "young": "YOUNG", + "shear": "SHEAR", + "bulk": "BULK", + "totaldynamicporevolume": "TDPORV", + "time": "TIME", + "dt": "DT", + "meanbhp": "MBHP", + "meantotalmassrate": "MTMR", + "meantotalvolumetricrate": "MTSVR", + "bhp": "BHP", + "totalmassrate": "TMR", + "cumulatedlineariter": "CLI", + "cumulatednewtoniter": "CNI", + "lineariter": "LI", + "newtoniter": "NI", +} + +phasesAssociations: dict[str, str] = { + "dissolvedmass": " IN ", + "immobile": "IMOB ", + "mobile": "MOB ", + "nontrapped": "NTRP ", + "dynamicporevolume": "DPORV ", + "meansurfacevolumetricrate": "MSVR ", + "surfacevolumetricrate": "SVR ", +} + + +def smartLabelsSorted( + labels: list[str], lines: list[lines.Line2D], userChoices: dict[str, Any] +) -> tuple[list[str], list[lines.Line2D]]: + """Shorten all legend labels and sort them. + + To improve readability of the legend for an axe in ParaView, we can apply the + smartLegendLabel functionnality to reduce the size of each label. Plus we sort them + alphabetically and therefore, we also sort the lines the same way. + + Args: + labels (list[str]): Labels to use ax.legend() like + ["Region1__TemperatureAvg__K__job_123456", "Region1__PressureMin__Pa__job_123456"] + lines (list[lines.Line2D]): Lines plotted on axes of matplotlib figure like [line1, line2] + userChoices (dict[str, Any]): Choices made by widget selection + in PythonViewConfigurator filter. + + Returns: + tuple[list[str], list[lines.Line2D]]: Improved labels and sorted labels / lines like + (["Region1 Pmin", "Region1 Tavg"], [line2, line1]) + """ + smartLabels: list[str] = [smartLabel(label, userChoices) for label in labels] + # I need the labels to be ordered alphabetically for better readability of the legend + # Therefore, if I sort smartLabels, I need to also sort lines with the same order. + # But this can only be done if there are no duplicates of labels in smartLabels. + # If a duplicate is found, "sorted" will try to sort with line which has no comparison built in + # which will throw an error. + if len(set(smartLabels)) == len(smartLabels): + sortedBothLists = sorted(zip(smartLabels, lines)) + sortedLabels, sortedLines = zip(*sortedBothLists) + return (list(sortedLabels), list(sortedLines)) + else: + return (smartLabels, lines) + + +def smartLabel(label: str, userChoices: dict[str, Any]) -> str: + """Shorten label according to user choices. + + Labels name can tend to be too long. Therefore, we need to reduce the size of the label. + Depending on the choices made by the user, the identifier and the job name can disappear. + + Args: + label (str): A label to be plotted. + Example- Reservoir__DissolvedMassphaseName0InphaseName1__kg__job123456.out + userChoices (dict[str, Any]): user choices. + + Returns: + str: "phaseName0 in phaseName1" or "Reservoir phaseName0 in phaseName1" + or "phaseName0 in phaseName1 job123456.out" or + "Reservoir phaseName0 in phaseName1 job123456.out" + """ + # first step is to abbreviate the label to reduce its size + smartLabel: str = abbreviateLabel(label) + # When only one source is used as input, there is no need to precise which one is used + # in the label so the job name is useless. Same when removeJobName option is selected by user. + inputNames: list[str] = userChoices["inputNames"] + removeJobName: bool = userChoices["removeJobName"] + if len(inputNames) > 1 and not removeJobName: + jobName: str = findJobName(label) + smartLabel += " " + jobName + # When the user chooses to split the plot into subplots to plot by region or well, + # this identifier name will appear as a title of the subplot so no need to use it. + # Same applies when user decides to remove regions. + plotRegions: bool = userChoices["plotRegions"] + removeRegions: bool = userChoices["removeRegions"] + if not plotRegions and not removeRegions: + smartLabel = findIdentifier(label) + " " + smartLabel + return smartLabel + + +def abbreviateLabel(label: str) -> str: + """Get the abbreviation of the label according to reservoir nomenclature. + + When using labels to plot, the name can tend to be too long. Therefore, to respect + the logic of reservoir engineering vocabulary, abbreviations for common property names + can be used to shorten the name. The goal is therefore to generate the right abbreviation + for the label input. + + Args: + label (str): A label to be plotted. + Example- Reservoir__DissolvedMassphaseName0InphaseName1__kg__job123456.out + + Returns: + str: "phaseName0 in phaseName1" + """ + for commonAsso in commonAssociations: + if commonAsso in label.lower(): + return commonAssociations[commonAsso] + for phaseAsso in phasesAssociations: + if phaseAsso in label.lower(): + phases: list[str] = findPhasesLabel(label) + phase0: str = "" if len(phases) < 1 else phases[0] + phase1: str = "" if len(phases) < 2 else phases[1] + if phaseAsso == "dissolvedmass": + return phase0 + phasesAssociations[phaseAsso] + phase1 + else: + return phasesAssociations[phaseAsso] + phase0 + return label + + +def findIdentifier(label: str) -> str: + """Find identifier inside the label. + + When looking at a label, it may contain or not an identifier at the beginning of it. + An identifier is either a regionName or a wellName. + The goal is to find it and extract it if present. + + Args: + label (str): A label to be plotted. + Example- Reservoir__DissolvedMassphaseName0InphaseName1__kg__job123456.out + + Returns: + str: "Reservoir" + """ + identifier: str = "" + if "__" not in label: + print("Invalid label, cannot search identifier when no '__' in label.") + return identifier + subParts: list[str] = label.split("__") + if len(subParts) == 4: + identifier = subParts[0] + return identifier + + +def findJobName(label: str) -> str: + """Find the Geos job name at the end of the label. + + When looking at a label, it may contain or not a job name at the end of it. + The goal is to find it and extract it if present. + + Args: + label (str): A label to be plotted. + Example- Reservoir__DissolvedMassphaseName0InphaseName1__kg__job123456.out + + Returns: + str: "job123456.out" + """ + jobName: str = "" + if "__" not in label: + print("Invalid label, cannot search jobName when no '__' in label.") + return jobName + subParts: list[str] = label.split("__") + if len(subParts) == 4: + jobName = subParts[3] + return jobName + + +def findPhasesLabel(label: str) -> list[str]: + """Find phase name inside label. + + When looking at a label, it may contain or not patterns that indicates + the presence of a phase name within it. Therefore, if one of these patterns + is present, one or multiple phase names can be found and be extracted. + + Args: + label (str): A label to be plotted. + Example- Reservoir__DissolvedMassphaseName0InphaseName1__kg__job123456.out + + Returns: + list[str]: [phaseName0, phaseName1] + """ + phases: list[str] = [] + lowLabel: str = label.lower() + indexStart: int = 0 + indexEnd: int = 0 + if "__" not in label: + print("Invalid label, cannot search phases when no '__' in label.") + return phases + if "dissolvedmass" in lowLabel: + indexStart = lowLabel.index("dissolvedmass") + len("dissolvedmass") + indexEnd = lowLabel.rfind("__") + phasesSubstring: str = lowLabel[indexStart:indexEnd] + phases = phasesSubstring.split("in") + phases = [phase.capitalize() for phase in phases] + else: + if "dynamicporevolume" in lowLabel: + indexStart = lowLabel.index("__") + 2 + indexEnd = lowLabel.index("dynamicporevolume") + else: + for pattern in ["nontrapped", "trapped", "immobile", "mobile", "rate"]: + if pattern in lowLabel: + indexStart = lowLabel.index(pattern) + len(pattern) + indexEnd = lowLabel.rfind("mass") + if indexEnd < 0: + indexEnd = indexStart + lowLabel[indexStart:].find("__") + break + if indexStart < indexEnd: + phases = [lowLabel[indexStart:indexEnd].capitalize()] + return phases + + +""" +Under this is the first version of smartLabels without abbreviations. +""" + +# def smartLegendLabelsAndLines( +# labelNames: list[str], lines: list[Any], userChoices: dict[str, Any], regionName="" +# ) -> tuple[list[str], list[Any]]: +# """To improve readability of the legend for an axe in ParaView, we can apply the +# smartLegendLabel functionnality to reduce the size of each label. Plus we sort them +# alphabetically and therefore, we also sort the lines the same way. + +# Args: +# labelNames (list[str]): Labels to use ax.legend() like +# ["Region1__PressureMin__Pa__job_123456", "Region1__Temperature__K__job_123456"] +# lines (list[Any]): Lines plotted on axes of matplotlib figure like [line1, line2] +# userChoices (dict[str, Any]): Choices made by widget selection +# in PythonViewConfigurator filter. +# regionName (str, optional): name of the region. Defaults to "". + +# Returns: +# tuple[list[str], list[Any]]: Improved labels and sorted labels / lines like +# (["Temperature K", "PressureMin Pa"], [line2, line1]) +# """ +# smartLabels: list[str] = [ +# smartLegendLabel(labelName, userChoices, regionName) for labelName in labelNames +# ] +# # I need the labels to be ordered alphabetically for better readability of the legend +# # Therefore, if I sort smartLabels, I need to also sort lines with the same order +# sortedBothLists = sorted(zip(smartLabels, lines) +# sortedLabels, sortedLines = zip(*sortedBothLists) +# return (sortedLabels, sortedLines) + + +# def smartLegendLabel(labelName: str, userChoices: dict[str, Any], regionName="") -> str: +# """When plotting legend label, the label format can be improved by removing some +# overwhelming / repetitive prefixe / suffixe and have a shorter label. + +# Args: +# labelName (str): Label to use ax.legend() like +# Region1__PressureMin__Pa__job_123456 +# userChoices (dict[str, Any]): Choices made by widget selection +# in PythonViewConfigurator filter. +# regionName (str, optional): name of the region. Defaults to "". + +# Returns: +# str: Improved label name like PressureMin Pa. +# """ +# smartLabel: str = "" +# # When only one source is used as input, there is no need to precise which one +# # is used in the label. Same when removeJobName option is selected by user. +# inputNames: list[str] = userChoices["inputNames"] +# removeJobName: bool = userChoices["removeJobName"] +# if len(inputNames) <= 1 or removeJobName: +# smartLabel = removeJobNameInLegendLabel(labelName, inputNames) +# # When the user chooses to split the plot into subplots to plot by region, +# # the region name will appear as a title of the subplot so no need to use it. +# # Same applies when user decides to remove regions. +# plotRegions: bool = userChoices["plotRegions"] +# removeRegions: bool = userChoices["removeRegions"] +# if plotRegions or removeRegions: +# smartLabel = removeIdentifierInLegendLabel(smartLabel, regionName) +# smartLabel = smartLabel.replace("__", " ") +# return smartLabel + + +# def removeJobNameInLegendLabel(legendLabel: str, inputNames: list[str]) -> str: +# """When plotting legends, the name of the job is by default at the end of +# the label. Therefore, it can increase tremendously the size of the legend +# and we can avoid that by removing the job name from it. + +# Args: +# legendLabel (str): Label to use ax.legend() like +# Region1__PressureMin__Pa__job_123456 +# inputNames (list[str]): names of the sources use to plot. + +# Returns: +# str: Label without the job name like Region1__PressureMin__Pa. +# """ +# for inputName in inputNames: +# pattern: str = "__" + inputName +# if legendLabel.endswith(pattern): +# jobIndex: int = legendLabel.index(pattern) +# return legendLabel[:jobIndex] +# return legendLabel + + +# def removeIdentifierInLegendLabel(legendLabel: str, regionName="") -> str: +# """When plotting legends, the name of the region is by default at the +# beginning of the label. Here we remove the region name from the legend label. + +# Args: +# legendLabel (str): Label to use ax.legend() like +# Region1__PressureMin__Pa__job_123456 +# regionName (str): name of the region. Defaults to "". + +# Returns: +# str: Label without the job name like PressureMin__Pa__job_123456 +# """ +# if "__" not in legendLabel: +# return legendLabel +# if regionName == "": +# firstRegionIndex: int = legendLabel.index("__") +# return legendLabel[firstRegionIndex + 2:] +# pattern: str = regionName + "__" +# if legendLabel.startswith(pattern): +# return legendLabel[len(pattern):] +# return legendLabel + + +""" +Other 2D tools for simplest figures +""" + + +def basicFigure( + df: pd.DataFrame, variableName: str, curveName: str +) -> tuple[figure.Figure, axes.Axes]: + """Creates a plot. + + Generates a figure and axes objects from matplotlib that plots + one curve along the X axis, with legend and label for X and Y. + + Args: + df (pd.DataFrame): dataframe containing at least two columns, + one named "variableName" and the other "curveName" + variableName (str): Name of the variable column + curveName (str): Name of the column to display along that variable. + + Returns: + tuple[figure.Figure, axes.Axes]: the fig and the ax. + """ + fig, ax = plt.subplots() + x: npt.NDArray[np.float64] = df[variableName].to_numpy() + y: npt.NDArray[np.float64] = df[curveName].to_numpy() + ax.plot(x, y, label=curveName) + ax.set_xlabel(variableName) + ax.set_ylabel(curveName) + ax.legend(loc="best") + return (fig, ax) + + +def invertedBasicFigure( + df: pd.DataFrame, variableName: str, curveName: str +) -> tuple[figure.Figure, axes.Axes]: + """Creates a plot with inverted XY axis. + + Generates a figure and axes objects from matplotlib that plots + one curve along the Y axis, with legend and label for X and Y. + + Args: + df (pd.DataFrame): dataframe containing at least two columns, + one named "variableName" and the other "curveName" + variableName (str): Name of the variable column + curveName (str): Name of the column to display along that variable. + + Returns: + tuple[figure.Figure, axes.Axes]: the fig and the ax. + """ + fig, ax = plt.subplots() + x: npt.NDArray[np.float64] = df[curveName].to_numpy() + y: npt.NDArray[np.float64] = df[variableName].to_numpy() + ax.plot(x, y, label=variableName) + ax.set_xlabel(curveName) + ax.set_ylabel(variableName) + ax.legend(loc="best") + return (fig, ax) + + +def adjust_subplots(fig: figure.Figure, invertXY: bool) -> figure.Figure: + """Adjust the size of the subplot in the fig. + + Args: + fig (figure.Figure): Matplotlib figure + invertXY (bool): Choice to either intervert or not the X and Y axes + + Returns: + figure.Figure: Matplotlib figure with adjustements + """ + if invertXY: + fig.subplots_adjust(left=0.05, right=0.98, top=0.9, bottom=0.2) + else: + fig.subplots_adjust(left=0.06, right=0.94, top=0.95, bottom=0.08) + return fig diff --git a/geos-posp/src/geos_posp/visu/pythonViewUtils/mainPythonView.py b/geos-posp/src/geos_posp/visu/pythonViewUtils/mainPythonView.py new file mode 100644 index 00000000..e211c72a --- /dev/null +++ b/geos-posp/src/geos_posp/visu/pythonViewUtils/mainPythonView.py @@ -0,0 +1,40 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# type: ignore +try: + import matplotlib.pyplot as plt + from paraview import python_view + + import geos_posp.visu.PVUtils.paraviewTreatments as pvt + from geos_posp.visu.pythonViewUtils.Figure2DGenerator import ( + Figure2DGenerator, + ) + + plt.close() + if len(sourceNames) == 0: # noqa: F821 + raise ValueError( + "No source name was found. Please check at least" + + " one source in <>" + ) + + dataframes = pvt.getDataframesFromMultipleVTKSources( + sourceNames, variableName # noqa: F821 + ) + dataframe = pvt.mergeDataframes(dataframes, variableName) # noqa: F821 + obj_figure = Figure2DGenerator(dataframe, userChoices) # noqa: F821 + fig = obj_figure.getFigure() + + def setup_data(view) -> None: # noqa + pass + + def render(view, width: int, height: int): # noqa + fig.set_size_inches(float(width) / 100.0, float(height) / 100.0) + imageToReturn = python_view.figure_to_image(fig) + return imageToReturn + +except Exception as e: + from geos_posp.utils.Logger import getLogger + + logger = getLogger("Python View Configurator") + logger.critical(e, exc_info=True) diff --git a/geos-posp/tests/Data/depleted_gas_reservoir_newwell_report.out b/geos-posp/tests/Data/depleted_gas_reservoir_newwell_report.out new file mode 100644 index 00000000..8175d459 --- /dev/null +++ b/geos-posp/tests/Data/depleted_gas_reservoir_newwell_report.out @@ -0,0 +1,28526 @@ +Num ranks: 1 +MKL max threads: 1 +GEOSX version: 0.2.0 (bugfix/rey/2320-xml-errors-feedback-4, sha1: 99abae2) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v4.0.3, package: Open MPI root@pandev01 Distribution, ident: 4.0.3, repo rev: v4.0.3, Mar 03, 2020 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.2.6 + - RAJA version: 2023.6.1 + - umpire version: 2023.6.0 + - adiak version: .. + - caliper version: 2.10.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 7.0.3 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - Python3 version: 3.9.13 + - hypre release version: 2.29.0 +Started at 2024-01-31 08:58:59.235079005 +Adding Solver of type CompositionalMultiphaseReservoir, named reservoirSystem +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: InternalMesh, mesh1 +Adding Mesh attribute: InternalWell, well_producer1 +Adding Mesh attribute: InternalWell, well_injector1 +Adding Event: PeriodicEvent, solverApplications +Adding Event: PeriodicEvent, outputs +Adding Event: PeriodicEvent, statistics + TableFunction: initC1CompFracTable + TableFunction: initCO2CompFracTable + TableFunction: initTempTable + TableFunction: producerSchedule + TableFunction: injectorSchedule +Adding Output: VTK, VTKOutput +Adding Object CellElementRegion named Region1 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion1 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion2 from ObjectManager::Catalog. +reservoirSystem: found SolverBase solver named compositionalMultiphaseFlow +reservoirSystem: found CompositionalMultiphaseWell solver named compositionalMultiphaseWell + TableFunction: wellControls1_ConstantBHP_table + TableFunction: wellControls1_ConstantTotalRate_table + TableFunction: wellControls1_ConstantPhaseRate_table + TableFunction: wellControls2_ConstantBHP_table + TableFunction: wellControls2_ConstantTotalRate_table + TableFunction: wellControls2_ConstantPhaseRate_table +mesh1: total number of nodes = 132651 +mesh1: total number of elems = 125000 +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh1, Level0, Region1, cb1 +mesh1/Level0/Region1/cb1/fluid1 allocated 1 quadrature points +mesh1/Level0/Region1/cb1/rock allocated 1 quadrature points +mesh1/Level0/Region1/cb1/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh1, Level0, wellRegion1, wellRegion1UniqueSubRegion +mesh1/Level0/wellRegion1/wellRegion1UniqueSubRegion/fluid1 allocated 1 quadrature points +mesh1/Level0/wellRegion1/wellRegion1UniqueSubRegion/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh1, Level0, wellRegion2, wellRegion2UniqueSubRegion +mesh1/Level0/wellRegion2/wellRegion2UniqueSubRegion/fluid1 allocated 1 quadrature points +mesh1/Level0/wellRegion2/wellRegion2UniqueSubRegion/relperm allocated 1 quadrature points +mesh1: importing field data from mesh dataset + TableFunction: equil_cb1_gas_table +Time: 0.00e+00 s, dt: 4320000 s, Cycle: 0 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.74e+01 ) ( Rwell ) = ( 7.52e+01 ) ( R ) = ( 1.08e+02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.0015582 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.789018 s | Solve Time: 0.0998169 s + compositionalMultiphaseFlow: Max pressure change: 1863728.007 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 67711.392 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.02651906699454667 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00954421442739195 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.53e+01 ) ( Rwell ) = ( 7.32e+01 ) ( R ) = ( 1.05e+02 ) + Last LinSolve(iter,res) = ( 1, 1.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00144494 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.613098 s | Solve Time: 0.0961314 s + compositionalMultiphaseFlow: Max pressure change: 1760321.056 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 15219.237 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.12521632240722028 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.011204661548812833 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.31e+01 ) ( Rwell ) = ( 6.40e+01 ) ( R ) = ( 9.72e+01 ) + Last LinSolve(iter,res) = ( 1, 1.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00126482 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589207 s | Solve Time: 0.095931 s + compositionalMultiphaseFlow: Max pressure change: 1510143.388 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5913.828 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.34724350561099404 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00885123892655415 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.45e+01 ) ( Rwell ) = ( 4.18e+01 ) ( R ) = ( 6.10e+01 ) + Last LinSolve(iter,res) = ( 1, 1.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.0015107 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572324 s | Solve Time: 0.096161 s + compositionalMultiphaseFlow: Max pressure change: 1101871.731 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1253.062 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.029105661622809587 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.30e+01 ) ( Rwell ) = ( 3.25e-03 ) ( R ) = ( 1.30e+01 ) + Last LinSolve(iter,res) = ( 1, 1.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.0863578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.575666 s | Solve Time: 22.0252 s + compositionalMultiphaseFlow: Max pressure change: 2012921856.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 419020600.000 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7245.046809648873 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.25e+03 ) ( Rwell ) = ( 2.13e-01 ) ( R ) = ( 7.25e+03 ) + Last LinSolve(iter,res) = ( 200, 8.64e-02 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6677.493797145663 + Line search @ 0.005: ( Rflow ) = ( 3.48e+03 ) ( Rwell ) = ( 5.35e-02 ) ( R ) = ( 3.48e+03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 425.34899505180135 + Line search @ 0.003: ( Rflow ) = ( 2.35e+03 ) ( Rwell ) = ( 9.54e-03 ) ( R ) = ( 2.35e+03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 342.15645699827087 + Line search @ 0.001: ( Rflow ) = ( 2.02e+03 ) ( Rwell ) = ( 5.12e-03 ) ( R ) = ( 2.02e+03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 227.8462312155841 + Line search @ 0.001: ( Rflow ) = ( 1.92e+03 ) ( Rwell ) = ( 2.91e-03 ) ( R ) = ( 1.92e+03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00639144 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.576053 s | Solve Time: 0.0948083 s + compositionalMultiphaseFlow: Max pressure change: 695197.019 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3772288.400 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.39082846938482624 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 567.2735333660391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e+03 ) ( Rwell ) = ( 1.70e-03 ) ( R ) = ( 1.17e+03 ) + Last LinSolve(iter,res) = ( 1, 6.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00923434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578621 s | Solve Time: 0.414541 s + compositionalMultiphaseFlow: Max pressure change: 506916.610 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2238516.485 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.34919349244121356 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 304.9156693692065 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.63e+02 ) ( Rwell ) = ( 1.09e-03 ) ( R ) = ( 7.63e+02 ) + Last LinSolve(iter,res) = ( 5, 9.23e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 15 | Final Rel Res: 0.00676409 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580377 s | Solve Time: 1.25498 s + compositionalMultiphaseFlow: Max pressure change: 496432.891 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1421965.794 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.05645914129670779 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 31.396445423115324 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.20e+02 ) ( Rwell ) = ( 1.03e-03 ) ( R ) = ( 7.20e+02 ) + Last LinSolve(iter,res) = ( 15, 6.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00971639 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.576369 s | Solve Time: 0.497155 s + compositionalMultiphaseFlow: Max pressure change: 473005.094 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1336273.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03157959293714468 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 16.539831835821133 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.97e+02 ) ( Rwell ) = ( 9.98e-04 ) ( R ) = ( 6.97e+02 ) + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00745442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.575825 s | Solve Time: 0.415492 s + compositionalMultiphaseFlow: Max pressure change: 467774.275 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1291954.451 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.09130079976165452 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 46.431693375286045 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.33e+02 ) ( Rwell ) = ( 9.05e-04 ) ( R ) = ( 6.33e+02 ) + Last LinSolve(iter,res) = ( 5, 7.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00768396 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578517 s | Solve Time: 0.496889 s + compositionalMultiphaseFlow: Max pressure change: 455482.610 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1168200.867 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0576316179770106 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 26.58392157984406 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.97e+02 ) ( Rwell ) = ( 8.53e-04 ) ( R ) = ( 5.97e+02 ) + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00967122 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577506 s | Solve Time: 0.661671 s + compositionalMultiphaseFlow: Max pressure change: 474058.043 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1097055.793 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03227034433272967 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 14.015024504220378 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.78e+02 ) ( Rwell ) = ( 8.25e-04 ) ( R ) = ( 5.78e+02 ) + Last LinSolve(iter,res) = ( 8, 9.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00623709 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579446 s | Solve Time: 1.17193 s + compositionalMultiphaseFlow: Max pressure change: 449008.501 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1060498.994 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.08656200248060067 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 36.44806302673902 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.28e+02 ) ( Rwell ) = ( 7.52e-04 ) ( R ) = ( 5.28e+02 ) + Last LinSolve(iter,res) = ( 14, 6.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00943427 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577228 s | Solve Time: 0.496676 s + compositionalMultiphaseFlow: Max pressure change: 426269.687 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 963854.055 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0480367075068047 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 18.438890842124636 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.02e+02 ) ( Rwell ) = ( 7.16e-04 ) ( R ) = ( 5.02e+02 ) + Last LinSolve(iter,res) = ( 6, 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.009068 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573573 s | Solve Time: 0.661338 s + compositionalMultiphaseFlow: Max pressure change: 414273.852 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 914324.375 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03978601388574054 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 14.53085734658299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.82e+02 ) ( Rwell ) = ( 6.87e-04 ) ( R ) = ( 4.82e+02 ) + Last LinSolve(iter,res) = ( 8, 9.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00486376 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577911 s | Solve Time: 0.495695 s + compositionalMultiphaseFlow: Max pressure change: 409709.349 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 876701.964 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.09417369701267622 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 33.09855714124973 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.37e+02 ) ( Rwell ) = ( 6.21e-04 ) ( R ) = ( 4.37e+02 ) + Last LinSolve(iter,res) = ( 6, 4.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00760883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578276 s | Solve Time: 0.254229 s + compositionalMultiphaseFlow: Max pressure change: 390203.969 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 789519.511 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.05204735204503805 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 16.53386542679874 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.14e+02 ) ( Rwell ) = ( 5.89e-04 ) ( R ) = ( 4.14e+02 ) + Last LinSolve(iter,res) = ( 3, 7.61e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00286386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578025 s | Solve Time: 0.415276 s + compositionalMultiphaseFlow: Max pressure change: 380964.163 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 746600.864 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.36473154507406386 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 111.06066839368654 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.63e+02 ) ( Rwell ) = ( 3.62e-04 ) ( R ) = ( 2.63e+02 ) + Last LinSolve(iter,res) = ( 5, 2.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00688061 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579191 s | Solve Time: 0.497548 s + compositionalMultiphaseFlow: Max pressure change: 312748.835 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 462131.150 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.37442790885864735 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 71.75306795005318 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.65e+02 ) ( Rwell ) = ( 2.24e-04 ) ( R ) = ( 1.65e+02 ) + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 18 | Final Rel Res: 0.00751689 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.57676 s | Solve Time: 1.51986 s + compositionalMultiphaseFlow: Max pressure change: 262564.258 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 282230.032 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.2623557757494769 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 31.09402559441618 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 20 + ( Rflow ) = ( 1.22e+02 ) ( Rwell ) = ( 1.67e-04 ) ( R ) = ( 1.22e+02 ) + Last LinSolve(iter,res) = ( 18, 7.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00589513 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577135 s | Solve Time: 0.334026 s + compositionalMultiphaseFlow: Max pressure change: 217524.653 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 206000.369 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.40968618712692834 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 35.8155101675901 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 21 + ( Rflow ) = ( 7.19e+01 ) ( Rwell ) = ( 1.06e-04 ) ( R ) = ( 7.19e+01 ) + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 17 | Final Rel Res: 0.00829661 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.574809 s | Solve Time: 1.43631 s + compositionalMultiphaseFlow: Max pressure change: 171707.794 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 119755.908 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.45936995461983293 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 23.54550751953047 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 22 + ( Rflow ) = ( 3.89e+01 ) ( Rwell ) = ( 6.72e-05 ) ( R ) = ( 3.89e+01 ) + Last LinSolve(iter,res) = ( 17, 8.30e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00803269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.574109 s | Solve Time: 0.744218 s + compositionalMultiphaseFlow: Max pressure change: 125328.408 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 64019.459 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.5270865775459574 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 14.500318922860961 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 23 + ( Rflow ) = ( 1.84e+01 ) ( Rwell ) = ( 4.09e-05 ) ( R ) = ( 1.84e+01 ) + Last LinSolve(iter,res) = ( 9, 8.03e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 17 | Final Rel Res: 0.00277094 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577287 s | Solve Time: 1.43519 s + compositionalMultiphaseFlow: Max pressure change: 88020.661 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29846.460 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.550690381195893 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.100674988640547 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 24 + ( Rflow ) = ( 8.30e+00 ) ( Rwell ) = ( 2.34e-05 ) ( R ) = ( 8.30e+00 ) + Last LinSolve(iter,res) = ( 17, 2.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00323333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.575408 s | Solve Time: 0.414409 s + compositionalMultiphaseFlow: Max pressure change: 55551.130 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13928.655 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.6372657666204999 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.6689818197272093 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 25 + ( Rflow ) = ( 3.03e+00 ) ( Rwell ) = ( 1.09e-05 ) ( R ) = ( 3.03e+00 ) + Last LinSolve(iter,res) = ( 5, 3.23e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00711024 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.575329 s | Solve Time: 0.578632 s + compositionalMultiphaseFlow: Max pressure change: 27361.714 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5382.724 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.9680896186568326 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9914849397422036 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 26 + ( Rflow ) = ( 1.37e-01 ) ( Rwell ) = ( 1.61e-06 ) ( R ) = ( 1.37e-01 ) + Last LinSolve(iter,res) = ( 7, 7.11e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00590897 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570321 s | Solve Time: 0.998591 s + compositionalMultiphaseFlow: Max pressure change: 2836.580 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 357.717 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.09155160772250492 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 27 + ( Rflow ) = ( 2.65e-02 ) ( Rwell ) = ( 1.41e-08 ) ( R ) = ( 2.65e-02 ) + Last LinSolve(iter,res) = ( 12, 5.91e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00442508 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567474 s | Solve Time: 0.254701 s + compositionalMultiphaseFlow: Max pressure change: 301.997 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 65.028 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.01839201833181936 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 28 + ( Rflow ) = ( 8.95e-05 ) ( Rwell ) = ( 5.20e-12 ) ( R ) = ( 8.95e-05 ) + Last LinSolve(iter,res) = ( 3, 4.43e-03 ) +wellControls1: BHP (at the specified reference elevation): 5921208.866098344 Pa +wellControls1: Total rate: -979.5821830738179 mol/s; total surface volumetric rate: -23.14814814802786 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814802786 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 19.190 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in more than 10 iterations, time-step required will be decreased. +compflowStatistics, Region1: Pressure (min, average, max): 9.15462e+06, 1.12618e+07, 1.15556e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.85579e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.28369e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.42742e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.85579e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.82724e+12, 2.85579e+10 } } mol +Time: 4.32e+06 s, dt: 2160000 s, Cycle: 1 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-01 ) ( Rwell ) = ( 1.23e-08 ) ( R ) = ( 1.21e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00874571 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573035 s | Solve Time: 0.334117 s + compositionalMultiphaseFlow: Max pressure change: 39100.017 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.319 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.453940945836621e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-03 ) ( Rwell ) = ( 4.52e-07 ) ( R ) = ( 2.35e-03 ) + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00166076 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570858 s | Solve Time: 0.333305 s + compositionalMultiphaseFlow: Max pressure change: 38.203 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.216 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0672543493406295e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-06 ) ( Rwell ) = ( 1.06e-10 ) ( R ) = ( 2.78e-06 ) + Last LinSolve(iter,res) = ( 4, 1.66e-03 ) +wellControls1: BHP (at the specified reference elevation): 5866232.912982572 Pa +wellControls1: Total rate: -979.58218290321 mol/s; total surface volumetric rate: -23.148148148836096 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148836096 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.427 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.1155e+06, 1.12536e+07, 1.15513e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.17398e+06, -1364.69 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.85368e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.28052e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.42563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.85368e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.82514e+12, 2.85368e+10 } } mol +Time: 6.48e+06 s, dt: 4320000 s, Cycle: 2 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.79e-03 ) ( Rwell ) = ( 4.06e-10 ) ( R ) = ( 8.79e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00476577 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571391 s | Solve Time: 0.333281 s + compositionalMultiphaseFlow: Max pressure change: 34633.342 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.014 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0986729281903251e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ( Rwell ) = ( 3.57e-07 ) ( R ) = ( 1.78e-03 ) + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0037411 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573971 s | Solve Time: 0.333028 s + compositionalMultiphaseFlow: Max pressure change: 35.692 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.158 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0978677278394855e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.60e-06 ) ( Rwell ) = ( 3.51e-10 ) ( R ) = ( 7.60e-06 ) + Last LinSolve(iter,res) = ( 4, 3.74e-03 ) +wellControls1: BHP (at the specified reference elevation): 5817397.353810271 Pa +wellControls1: Total rate: -979.5821815120917 mol/s; total surface volumetric rate: -23.148148147840146 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147840146 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.380 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.08083e+06, 1.12371e+07, 1.15374e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.21309e+06, -2582.51 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.84945e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.27417e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.42203e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.84945e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.82095e+12, 2.84945e+10 } } mol +Time: 1.08e+07 s, dt: 4320000 s, Cycle: 3 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-03 ) ( Rwell ) = ( 4.88e-10 ) ( R ) = ( 3.91e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00242189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569631 s | Solve Time: 0.329785 s + compositionalMultiphaseFlow: Max pressure change: 27595.370 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 8.798 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.145979563638605e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-03 ) ( Rwell ) = ( 2.30e-07 ) ( R ) = ( 1.62e-03 ) + Last LinSolve(iter,res) = ( 4, 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00794465 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.56862 s | Solve Time: 0.251215 s + compositionalMultiphaseFlow: Max pressure change: 17.353 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.116 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.169547777685636e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-05 ) ( Rwell ) = ( 4.10e-10 ) ( R ) = ( 1.25e-05 ) + Last LinSolve(iter,res) = ( 3, 7.94e-03 ) +wellControls1: BHP (at the specified reference elevation): 5778426.677081468 Pa +wellControls1: Total rate: -979.5821826324857 mol/s; total surface volumetric rate: -23.148148148145026 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148145026 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.304 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.05322e+06, 1.12207e+07, 1.15205e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.24776e+06, -7704.2 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.84521e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.26782e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.41843e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.84521e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.81676e+12, 2.84521e+10 } } mol +Time: 1.51e+07 s, dt: 4320000 s, Cycle: 4 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.13e-03 ) ( Rwell ) = ( 3.05e-10 ) ( R ) = ( 3.13e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00239413 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570775 s | Solve Time: 0.330105 s + compositionalMultiphaseFlow: Max pressure change: 24706.404 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.881 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.727310181669054e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 1.87e-07 ) ( R ) = ( 1.35e-03 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00979957 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567258 s | Solve Time: 0.250957 s + compositionalMultiphaseFlow: Max pressure change: 14.582 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.101 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.7319025414948044e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-05 ) ( Rwell ) = ( 6.33e-10 ) ( R ) = ( 1.30e-05 ) + Last LinSolve(iter,res) = ( 3, 9.80e-03 ) +wellControls1: BHP (at the specified reference elevation): 5743480.012870796 Pa +wellControls1: Total rate: -979.5821823654388 mol/s; total surface volumetric rate: -23.14814814817215 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814817215 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.273 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.0285e+06, 1.12043e+07, 1.15022e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.27537e+06, -15270.2 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.84098e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.26147e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.41483e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.84098e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.81257e+12, 2.84098e+10 } } mol +Time: 1.94e+07 s, dt: 4320000 s, Cycle: 5 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.81e-03 ) ( Rwell ) = ( 5.39e-10 ) ( R ) = ( 2.81e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00225785 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.56676 s | Solve Time: 0.330292 s + compositionalMultiphaseFlow: Max pressure change: 23192.954 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.394 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.459198326729364e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 1.67e-07 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 2.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00987669 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.566717 s | Solve Time: 0.251238 s + compositionalMultiphaseFlow: Max pressure change: 10.433 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.461912111481837e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-05 ) ( Rwell ) = ( 6.98e-10 ) ( R ) = ( 1.11e-05 ) + Last LinSolve(iter,res) = ( 3, 9.88e-03 ) +wellControls1: BHP (at the specified reference elevation): 5710629.29594418 Pa +wellControls1: Total rate: -979.5821821172459 mol/s; total surface volumetric rate: -23.14814814800035 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814800035 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.257 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.00529e+06, 1.11879e+07, 1.14832e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.30009e+06, -24769.3 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.83675e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.25513e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.41124e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.83675e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.80838e+12, 2.83675e+10 } } mol +Time: 2.38e+07 s, dt: 4320000 s, Cycle: 6 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-03 ) ( Rwell ) = ( 6.10e-10 ) ( R ) = ( 2.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00262677 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568544 s | Solve Time: 0.330263 s + compositionalMultiphaseFlow: Max pressure change: 22316.885 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.114 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.491245180788695e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 1.56e-07 ) ( R ) = ( 1.27e-03 ) + Last LinSolve(iter,res) = ( 4, 2.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0026997 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570457 s | Solve Time: 0.329794 s + compositionalMultiphaseFlow: Max pressure change: 8.686 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.109 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.467749031318192e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-06 ) ( Rwell ) = ( 1.08e-10 ) ( R ) = ( 1.61e-06 ) + Last LinSolve(iter,res) = ( 4, 2.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 5678975.905495109 Pa +wellControls1: Total rate: -979.5821815959824 mol/s; total surface volumetric rate: -23.148148148764918 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148764918 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.248 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.98297e+06, 1.11715e+07, 1.14642e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.3233e+06, -35708.9 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.83252e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.24878e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.40764e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.83252e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.80419e+12, 2.83252e+10 } } mol +Time: 2.81e+07 s, dt: 3480000 s, Cycle: 7 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-03 ) ( Rwell ) = ( 1.98e-10 ) ( R ) = ( 2.05e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00188658 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569954 s | Solve Time: 0.329524 s + compositionalMultiphaseFlow: Max pressure change: 17606.318 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.612 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.480231658414823e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-04 ) ( Rwell ) = ( 9.82e-08 ) ( R ) = ( 6.14e-04 ) + Last LinSolve(iter,res) = ( 4, 1.89e-03 ) +wellControls1: BHP (at the specified reference elevation): 5653991.504817751 Pa +wellControls1: Total rate: -979.5821583182151 mol/s; total surface volumetric rate: -23.14814815085941 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814815085941 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.196 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.96536e+06, 1.11583e+07, 1.14489e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.34562e+06, -47703.9 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.82911e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.24366e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.40474e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.82911e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.80082e+12, 2.8291e+10 } } mol +Time: 3.16e+07 s, dt: 4320000 s, Cycle: 8 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.28e-03 ) ( Rwell ) = ( 9.87e-08 ) ( R ) = ( 2.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00261289 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572611 s | Solve Time: 0.329749 s + compositionalMultiphaseFlow: Max pressure change: 21487.760 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.854 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8177673366537306e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 1.48e-07 ) ( R ) = ( 1.20e-03 ) + Last LinSolve(iter,res) = ( 4, 2.61e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00278297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567073 s | Solve Time: 0.330002 s + compositionalMultiphaseFlow: Max pressure change: 6.698 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.107 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.296172500557361e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-06 ) ( Rwell ) = ( 1.25e-10 ) ( R ) = ( 1.65e-06 ) + Last LinSolve(iter,res) = ( 4, 2.78e-03 ) +wellControls1: BHP (at the specified reference elevation): 5623426.850695061 Pa +wellControls1: Total rate: -979.5821651376788 mol/s; total surface volumetric rate: -23.14814814789728 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814789728 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.240 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.94387e+06, 1.11419e+07, 1.143e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.36323e+06, -57897.8 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.82488e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.23732e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.40115e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.82488e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.79663e+12, 2.82487e+10 } } mol +Time: 3.59e+07 s, dt: 4320000 s, Cycle: 9 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.46e-03 ) ( Rwell ) = ( 2.13e-10 ) ( R ) = ( 2.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00264823 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.575412 s | Solve Time: 0.35037 s + compositionalMultiphaseFlow: Max pressure change: 21236.632 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.777 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.1706714021548805e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 1.46e-07 ) ( R ) = ( 1.23e-03 ) + Last LinSolve(iter,res) = ( 4, 2.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00286792 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569881 s | Solve Time: 0.330326 s + compositionalMultiphaseFlow: Max pressure change: 6.840 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.106 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.17037290759248e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-06 ) ( Rwell ) = ( 1.38e-10 ) ( R ) = ( 1.69e-06 ) + Last LinSolve(iter,res) = ( 4, 2.87e-03 ) +wellControls1: BHP (at the specified reference elevation): 5593191.608551039 Pa +wellControls1: Total rate: -979.5821729876623 mol/s; total surface volumetric rate: -23.148148147928673 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147928673 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.238 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.92262e+06, 1.11254e+07, 1.14114e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.38472e+06, -71164.6 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.82065e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.23097e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.39755e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.82065e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.79244e+12, 2.82064e+10 } } mol +Time: 4.02e+07 s, dt: 4320000 s, Cycle: 10 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.44e-03 ) ( Rwell ) = ( 2.25e-10 ) ( R ) = ( 2.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00262109 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568303 s | Solve Time: 0.330413 s + compositionalMultiphaseFlow: Max pressure change: 21068.643 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.719 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.9877601604464417e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 1.45e-07 ) ( R ) = ( 1.20e-03 ) + Last LinSolve(iter,res) = ( 4, 2.62e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00291064 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568313 s | Solve Time: 0.329601 s + compositionalMultiphaseFlow: Max pressure change: 6.443 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.104 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.9853953631995296e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-06 ) ( Rwell ) = ( 1.47e-10 ) ( R ) = ( 1.63e-06 ) + Last LinSolve(iter,res) = ( 4, 2.91e-03 ) +wellControls1: BHP (at the specified reference elevation): 5563154.249840551 Pa +wellControls1: Total rate: -979.5821769592776 mol/s; total surface volumetric rate: -23.148148148098183 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148098183 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.236 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.90155e+06, 1.1109e+07, 1.1393e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.40597e+06, -84899.8 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.81641e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.22462e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.39395e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.81641e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.78825e+12, 2.81641e+10 } } mol +Time: 4.45e+07 s, dt: 4320000 s, Cycle: 11 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-03 ) ( Rwell ) = ( 2.34e-10 ) ( R ) = ( 2.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236047 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568154 s | Solve Time: 0.330976 s + compositionalMultiphaseFlow: Max pressure change: 20948.054 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.680 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.853035417973217e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 1.45e-07 ) ( R ) = ( 1.14e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252893 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569076 s | Solve Time: 0.330276 s + compositionalMultiphaseFlow: Max pressure change: 7.638 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.097 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.853131807536215e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-06 ) ( Rwell ) = ( 9.84e-11 ) ( R ) = ( 1.28e-06 ) + Last LinSolve(iter,res) = ( 4, 2.53e-03 ) +wellControls1: BHP (at the specified reference elevation): 5533245.805902412 Pa +wellControls1: Total rate: -979.5821787495179 mol/s; total surface volumetric rate: -23.148148148037208 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148037208 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.88059e+06, 1.10926e+07, 1.13748e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.42704e+06, -99001.3 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.81218e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.21827e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.39036e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.81218e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.78406e+12, 2.81218e+10 } } mol +Time: 4.88e+07 s, dt: 4320000 s, Cycle: 12 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 1.86e-10 ) ( R ) = ( 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00258941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.574194 s | Solve Time: 0.330286 s + compositionalMultiphaseFlow: Max pressure change: 20862.175 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.653 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.740625736410209e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 1.45e-07 ) ( R ) = ( 1.26e-03 ) + Last LinSolve(iter,res) = ( 4, 2.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00274838 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572781 s | Solve Time: 0.330419 s + compositionalMultiphaseFlow: Max pressure change: 6.629 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.103 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.7431057970115376e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-06 ) ( Rwell ) = ( 1.18e-10 ) ( R ) = ( 1.50e-06 ) + Last LinSolve(iter,res) = ( 4, 2.75e-03 ) +wellControls1: BHP (at the specified reference elevation): 5503420.409652205 Pa +wellControls1: Total rate: -979.5821794316812 mol/s; total surface volumetric rate: -23.148148148441212 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148441212 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.85972e+06, 1.10762e+07, 1.13568e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.448e+06, -113395 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.80795e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.21193e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.38676e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.80795e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.77987e+12, 2.80795e+10 } } mol +Time: 5.32e+07 s, dt: 4320000 s, Cycle: 13 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-03 ) ( Rwell ) = ( 2.06e-10 ) ( R ) = ( 2.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571423 s | Solve Time: 0.334766 s + compositionalMultiphaseFlow: Max pressure change: 20796.847 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.630 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.617732396461349e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 1.45e-07 ) ( R ) = ( 1.15e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571075 s | Solve Time: 0.330192 s + compositionalMultiphaseFlow: Max pressure change: 7.561 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.097 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.6179136514723496e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-06 ) ( Rwell ) = ( 9.84e-11 ) ( R ) = ( 1.25e-06 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) +wellControls1: BHP (at the specified reference elevation): 5473646.170081585 Pa +wellControls1: Total rate: -979.5821795973161 mol/s; total surface volumetric rate: -23.1481481484771 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.1481481484771 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.83892e+06, 1.10598e+07, 1.13389e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.46887e+06, -128026 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.80372e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.20558e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.38316e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.80372e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.77568e+12, 2.80372e+10 } } mol +Time: 5.75e+07 s, dt: 4320000 s, Cycle: 14 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-03 ) ( Rwell ) = ( 1.87e-10 ) ( R ) = ( 2.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235215 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569221 s | Solve Time: 0.330731 s + compositionalMultiphaseFlow: Max pressure change: 20748.386 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.615 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.509575712852154e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 1.46e-07 ) ( R ) = ( 1.15e-03 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0025242 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568223 s | Solve Time: 0.330809 s + compositionalMultiphaseFlow: Max pressure change: 7.672 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.510585482897511e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-06 ) ( Rwell ) = ( 9.53e-11 ) ( R ) = ( 1.23e-06 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) +wellControls1: BHP (at the specified reference elevation): 5443900.221978691 Pa +wellControls1: Total rate: -979.5821794981288 mol/s; total surface volumetric rate: -23.14814814801823 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814801823 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.81816e+06, 1.10434e+07, 1.13212e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.48967e+06, -142851 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.79949e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.19923e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.37956e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.79949e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.77149e+12, 2.79949e+10 } } mol +Time: 6.18e+07 s, dt: 1320000 s, Cycle: 15 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.37e-04 ) ( Rwell ) = ( 1.84e-10 ) ( R ) = ( 7.37e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00657193 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5683 s | Solve Time: 0.25165 s + compositionalMultiphaseFlow: Max pressure change: 6327.382 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.067 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.616923288125463e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-04 ) ( Rwell ) = ( 1.37e-08 ) ( R ) = ( 4.86e-04 ) + Last LinSolve(iter,res) = ( 3, 6.57e-03 ) +wellControls1: BHP (at the specified reference elevation): 5434835.445374028 Pa +wellControls1: Total rate: -979.5822312069783 mol/s; total surface volumetric rate: -23.14814814610394 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814610394 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.072 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.81184e+06, 1.10384e+07, 1.13158e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.51043e+06, -157837 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.79819e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.19729e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.37847e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.79819e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.77021e+12, 2.7982e+10 } } mol +Time: 6.31e+07 s, dt: 2640000 s, Cycle: 16 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ( Rwell ) = ( 1.38e-08 ) ( R ) = ( 1.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00169888 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572527 s | Solve Time: 0.330611 s + compositionalMultiphaseFlow: Max pressure change: 12674.055 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.010 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2312432406957896e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.80e-04 ) ( Rwell ) = ( 5.57e-08 ) ( R ) = ( 2.80e-04 ) + Last LinSolve(iter,res) = ( 4, 1.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 5416640.404166159 Pa +wellControls1: Total rate: -979.5821789266862 mol/s; total surface volumetric rate: -23.148148152646325 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148152646325 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.79916e+06, 1.10284e+07, 1.1305e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.51675e+06, -162431 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.79561e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.19341e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.37627e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.79561e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.76765e+12, 2.79561e+10 } } mol +Time: 6.58e+07 s, dt: 4320000 s, Cycle: 17 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.28e-03 ) ( Rwell ) = ( 5.60e-08 ) ( R ) = ( 2.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00229097 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567945 s | Solve Time: 0.330783 s + compositionalMultiphaseFlow: Max pressure change: 20687.681 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.594 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.745811245041807e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 1.48e-07 ) ( R ) = ( 1.15e-03 ) + Last LinSolve(iter,res) = ( 4, 2.29e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00243493 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571532 s | Solve Time: 0.330894 s + compositionalMultiphaseFlow: Max pressure change: 6.833 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.349999516151115e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-06 ) ( Rwell ) = ( 1.03e-10 ) ( R ) = ( 1.16e-06 ) + Last LinSolve(iter,res) = ( 4, 2.43e-03 ) +wellControls1: BHP (at the specified reference elevation): 5386896.282499451 Pa +wellControls1: Total rate: -979.5821787475494 mol/s; total surface volumetric rate: -23.14814814806157 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814806157 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.77847e+06, 1.1012e+07, 1.12876e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.52943e+06, -171667 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.79138e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.18706e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.37267e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.79138e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.76346e+12, 2.79138e+10 } } mol +Time: 7.01e+07 s, dt: 4320000 s, Cycle: 18 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 1.92e-10 ) ( R ) = ( 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00263203 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568753 s | Solve Time: 0.330451 s + compositionalMultiphaseFlow: Max pressure change: 20665.613 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.589 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.248607465839882e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 1.49e-07 ) ( R ) = ( 1.23e-03 ) + Last LinSolve(iter,res) = ( 4, 2.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00295229 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571718 s | Solve Time: 0.33043 s + compositionalMultiphaseFlow: Max pressure change: 6.463 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.101 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.2443791592461366e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-06 ) ( Rwell ) = ( 1.55e-10 ) ( R ) = ( 1.61e-06 ) + Last LinSolve(iter,res) = ( 4, 2.95e-03 ) +wellControls1: BHP (at the specified reference elevation): 5357150.960966276 Pa +wellControls1: Total rate: -979.5821798738334 mol/s; total surface volumetric rate: -23.1481481480157 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.1481481480157 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.7578e+06, 1.09956e+07, 1.12702e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.55012e+06, -186897 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.78714e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.18072e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.36907e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.78714e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.75927e+12, 2.78715e+10 } } mol +Time: 7.44e+07 s, dt: 4320000 s, Cycle: 19 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 2.45e-10 ) ( R ) = ( 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0023521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.57108 s | Solve Time: 0.33019 s + compositionalMultiphaseFlow: Max pressure change: 20649.858 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.583 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.195018465935618e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-03 ) ( Rwell ) = ( 1.51e-07 ) ( R ) = ( 1.18e-03 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00250167 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5724 s | Solve Time: 0.330802 s + compositionalMultiphaseFlow: Max pressure change: 7.731 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.200078240756966e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-06 ) ( Rwell ) = ( 9.38e-11 ) ( R ) = ( 1.20e-06 ) + Last LinSolve(iter,res) = ( 4, 2.50e-03 ) +wellControls1: BHP (at the specified reference elevation): 5327384.632319523 Pa +wellControls1: Total rate: -979.5821795764831 mol/s; total surface volumetric rate: -23.14814814847537 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814847537 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.236 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.73714e+06, 1.09792e+07, 1.12529e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.57079e+06, -202223 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.78291e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.17437e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.36548e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.78291e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.75508e+12, 2.78292e+10 } } mol +Time: 7.87e+07 s, dt: 4320000 s, Cycle: 20 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 1.84e-10 ) ( R ) = ( 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236027 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569259 s | Solve Time: 0.330637 s + compositionalMultiphaseFlow: Max pressure change: 20640.408 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.579 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.1297890440716856e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 1.52e-07 ) ( R ) = ( 1.17e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00253815 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573833 s | Solve Time: 0.330371 s + compositionalMultiphaseFlow: Max pressure change: 7.222 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.128062180974723e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-06 ) ( Rwell ) = ( 1.08e-10 ) ( R ) = ( 1.19e-06 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) +wellControls1: BHP (at the specified reference elevation): 5297590.734637746 Pa +wellControls1: Total rate: -979.582178656356 mol/s; total surface volumetric rate: -23.148148147807273 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147807273 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.236 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.71649e+06, 1.09628e+07, 1.12357e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.59145e+06, -217630 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.77868e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.16802e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.36188e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.77868e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.75089e+12, 2.77869e+10 } } mol +Time: 8.30e+07 s, dt: 4320000 s, Cycle: 21 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-03 ) ( Rwell ) = ( 1.99e-10 ) ( R ) = ( 2.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00232174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572207 s | Solve Time: 0.330464 s + compositionalMultiphaseFlow: Max pressure change: 20634.947 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.576 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.0253154365288424e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 1.54e-07 ) ( R ) = ( 1.17e-03 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00250343 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568871 s | Solve Time: 0.330795 s + compositionalMultiphaseFlow: Max pressure change: 6.566 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.0243956167529404e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-06 ) ( Rwell ) = ( 9.54e-11 ) ( R ) = ( 1.19e-06 ) + Last LinSolve(iter,res) = ( 4, 2.50e-03 ) +wellControls1: BHP (at the specified reference elevation): 5267763.555794703 Pa +wellControls1: Total rate: -979.5821777463868 mol/s; total surface volumetric rate: -23.14814814833602 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814833602 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.69585e+06, 1.09464e+07, 1.12185e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.6121e+06, -233105 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.77445e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.16167e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.35828e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.77445e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.7467e+12, 2.77446e+10 } } mol +Time: 8.74e+07 s, dt: 4320000 s, Cycle: 22 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-03 ) ( Rwell ) = ( 1.87e-10 ) ( R ) = ( 2.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00239395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568884 s | Solve Time: 0.330908 s + compositionalMultiphaseFlow: Max pressure change: 20630.222 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.578 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.0015539770621444e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 1.55e-07 ) ( R ) = ( 1.19e-03 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00280322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571442 s | Solve Time: 0.330263 s + compositionalMultiphaseFlow: Max pressure change: 8.425 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.089 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.0015468938392473e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-06 ) ( Rwell ) = ( 1.20e-10 ) ( R ) = ( 1.24e-06 ) + Last LinSolve(iter,res) = ( 4, 2.80e-03 ) +wellControls1: BHP (at the specified reference elevation): 5237898.151531809 Pa +wellControls1: Total rate: -979.5821768418306 mol/s; total surface volumetric rate: -23.148148148030252 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148030252 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.67521e+06, 1.093e+07, 1.12014e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.63274e+06, -248638 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.77022e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.15533e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.35468e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.77022e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.74251e+12, 2.77023e+10 } } mol +Time: 9.17e+07 s, dt: 3000000 s, Cycle: 23 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-03 ) ( Rwell ) = ( 2.12e-10 ) ( R ) = ( 1.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00168696 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570452 s | Solve Time: 0.330151 s + compositionalMultiphaseFlow: Max pressure change: 14332.273 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.571 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8787918332208164e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.87e-04 ) ( Rwell ) = ( 7.57e-08 ) ( R ) = ( 4.87e-04 ) + Last LinSolve(iter,res) = ( 4, 1.69e-03 ) +wellControls1: BHP (at the specified reference elevation): 5217140.973682414 Pa +wellControls1: Total rate: -979.5821612236175 mol/s; total surface volumetric rate: -23.148148149470217 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148149470217 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.66088e+06, 1.09186e+07, 1.11895e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.65338e+06, -264221 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.76728e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.15092e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.35219e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.76728e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.73961e+12, 2.76728e+10 } } mol +Time: 9.47e+07 s, dt: 4320000 s, Cycle: 24 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.28e-03 ) ( Rwell ) = ( 7.61e-08 ) ( R ) = ( 2.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00238931 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571157 s | Solve Time: 0.330491 s + compositionalMultiphaseFlow: Max pressure change: 20634.742 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.580 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0655726462592838e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 1.58e-07 ) ( R ) = ( 1.21e-03 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00256437 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567902 s | Solve Time: 0.330696 s + compositionalMultiphaseFlow: Max pressure change: 7.334 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.945992754772476e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-06 ) ( Rwell ) = ( 1.19e-10 ) ( R ) = ( 1.34e-06 ) + Last LinSolve(iter,res) = ( 4, 2.56e-03 ) +wellControls1: BHP (at the specified reference elevation): 5187188.327017387 Pa +wellControls1: Total rate: -979.5821632315783 mol/s; total surface volumetric rate: -23.148148147659793 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147659793 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.238 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.64024e+06, 1.09022e+07, 1.11724e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.66771e+06, -275064 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.76305e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.14457e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.34859e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.76305e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.73542e+12, 2.76305e+10 } } mol +Time: 9.90e+07 s, dt: 4320000 s, Cycle: 25 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.45e-03 ) ( Rwell ) = ( 2.13e-10 ) ( R ) = ( 2.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259805 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.56943 s | Solve Time: 0.330847 s + compositionalMultiphaseFlow: Max pressure change: 20635.177 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.584 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.922750391183172e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-03 ) ( Rwell ) = ( 1.60e-07 ) ( R ) = ( 1.36e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00272326 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568501 s | Solve Time: 0.330372 s + compositionalMultiphaseFlow: Max pressure change: 7.399 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.919023905396557e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-06 ) ( Rwell ) = ( 1.03e-10 ) ( R ) = ( 1.40e-06 ) + Last LinSolve(iter,res) = ( 4, 2.72e-03 ) +wellControls1: BHP (at the specified reference elevation): 5157202.630387498 Pa +wellControls1: Total rate: -979.5821686620113 mol/s; total surface volumetric rate: -23.148148147767508 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147767508 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.239 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.61959e+06, 1.08858e+07, 1.11554e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.68835e+06, -290714 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.75881e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.13822e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.34499e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.75881e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.73123e+12, 2.75882e+10 } } mol +Time: 1.03e+08 s, dt: 4320000 s, Cycle: 26 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.45e-03 ) ( Rwell ) = ( 1.97e-10 ) ( R ) = ( 2.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259544 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573753 s | Solve Time: 0.332248 s + compositionalMultiphaseFlow: Max pressure change: 20640.751 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.584 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.881322130361298e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-03 ) ( Rwell ) = ( 1.62e-07 ) ( R ) = ( 1.36e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00269748 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.574282 s | Solve Time: 0.330284 s + compositionalMultiphaseFlow: Max pressure change: 7.500 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.889275834723094e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-06 ) ( Rwell ) = ( 1.02e-10 ) ( R ) = ( 1.39e-06 ) + Last LinSolve(iter,res) = ( 4, 2.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 5127164.625207989 Pa +wellControls1: Total rate: -979.5821712086042 mol/s; total surface volumetric rate: -23.148148148127273 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148127273 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.240 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.59894e+06, 1.08694e+07, 1.11384e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.709e+06, -306396 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.75458e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.13187e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.3414e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.75458e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.72704e+12, 2.75459e+10 } } mol +Time: 1.08e+08 s, dt: 4320000 s, Cycle: 27 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.46e-03 ) ( Rwell ) = ( 1.97e-10 ) ( R ) = ( 2.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259712 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573488 s | Solve Time: 0.330607 s + compositionalMultiphaseFlow: Max pressure change: 20647.732 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.585 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.8496743126614774e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-03 ) ( Rwell ) = ( 1.64e-07 ) ( R ) = ( 1.37e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00269583 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569505 s | Solve Time: 0.330713 s + compositionalMultiphaseFlow: Max pressure change: 7.549 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.8465712615121106e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-06 ) ( Rwell ) = ( 1.02e-10 ) ( R ) = ( 1.40e-06 ) + Last LinSolve(iter,res) = ( 4, 2.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 5097072.229692969 Pa +wellControls1: Total rate: -979.5821721945316 mol/s; total surface volumetric rate: -23.148148148113478 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148113478 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.240 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.57829e+06, 1.0853e+07, 1.11215e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.72965e+06, -322105 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.75035e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.12553e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.3378e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.75035e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.72285e+12, 2.75036e+10 } } mol +Time: 1.12e+08 s, dt: 4320000 s, Cycle: 28 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.47e-03 ) ( Rwell ) = ( 1.98e-10 ) ( R ) = ( 2.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00232398 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571601 s | Solve Time: 0.330186 s + compositionalMultiphaseFlow: Max pressure change: 20656.078 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.584 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.80189568716105e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 1.65e-07 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00238996 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569409 s | Solve Time: 0.33081 s + compositionalMultiphaseFlow: Max pressure change: 7.458 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7994254187267984e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-06 ) ( Rwell ) = ( 1.06e-10 ) ( R ) = ( 1.17e-06 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) +wellControls1: BHP (at the specified reference elevation): 5066923.442114172 Pa +wellControls1: Total rate: -979.5821724793293 mol/s; total surface volumetric rate: -23.148148148175853 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148175853 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.55763e+06, 1.08366e+07, 1.11045e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.7503e+06, -337836 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.74612e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.11918e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.3342e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.74612e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.71866e+12, 2.74613e+10 } } mol +Time: 1.16e+08 s, dt: 4320000 s, Cycle: 29 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-03 ) ( Rwell ) = ( 2.02e-10 ) ( R ) = ( 2.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00244295 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569503 s | Solve Time: 0.330689 s + compositionalMultiphaseFlow: Max pressure change: 20665.550 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.585 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.762294054077131e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 1.67e-07 ) ( R ) = ( 1.26e-03 ) + Last LinSolve(iter,res) = ( 4, 2.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00262827 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571143 s | Solve Time: 0.330284 s + compositionalMultiphaseFlow: Max pressure change: 7.311 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.101 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.764277201057098e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-06 ) ( Rwell ) = ( 1.07e-10 ) ( R ) = ( 1.29e-06 ) + Last LinSolve(iter,res) = ( 4, 2.63e-03 ) +wellControls1: BHP (at the specified reference elevation): 5036716.395022521 Pa +wellControls1: Total rate: -979.5821724615658 mol/s; total surface volumetric rate: -23.148148147964505 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147964505 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.242 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.53695e+06, 1.08202e+07, 1.10876e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.77096e+06, -353587 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.74189e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.11283e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.3306e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.74189e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.71447e+12, 2.7419e+10 } } mol +Time: 1.21e+08 s, dt: 4320000 s, Cycle: 30 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-03 ) ( Rwell ) = ( 2.04e-10 ) ( R ) = ( 2.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235083 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569471 s | Solve Time: 0.330043 s + compositionalMultiphaseFlow: Max pressure change: 20674.829 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.589 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.730589526185213e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 1.69e-07 ) ( R ) = ( 1.26e-03 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00244176 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570172 s | Solve Time: 0.33138 s + compositionalMultiphaseFlow: Max pressure change: 8.337 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7284404896809065e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-06 ) ( Rwell ) = ( 9.12e-11 ) ( R ) = ( 1.17e-06 ) + Last LinSolve(iter,res) = ( 4, 2.44e-03 ) +wellControls1: BHP (at the specified reference elevation): 5006449.298558478 Pa +wellControls1: Total rate: -979.582172345836 mol/s; total surface volumetric rate: -23.148148148173632 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148173632 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.242 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.51627e+06, 1.08038e+07, 1.10707e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.79164e+06, -369354 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.73766e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.10648e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.32701e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.73766e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.71028e+12, 2.73767e+10 } } mol +Time: 1.25e+08 s, dt: 1320000 s, Cycle: 31 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.61e-04 ) ( Rwell ) = ( 1.89e-10 ) ( R ) = ( 7.61e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0066845 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568859 s | Solve Time: 0.251843 s + compositionalMultiphaseFlow: Max pressure change: 6309.676 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.059 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.961899919247003e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.70e-04 ) ( Rwell ) = ( 1.59e-08 ) ( R ) = ( 4.70e-04 ) + Last LinSolve(iter,res) = ( 3, 6.68e-03 ) +wellControls1: BHP (at the specified reference elevation): 4997217.969852827 Pa +wellControls1: Total rate: -979.5822231256647 mol/s; total surface volumetric rate: -23.14814814664592 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814664592 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.50996e+06, 1.07988e+07, 1.10655e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.81232e+06, -385135 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.73636e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.10454e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.32591e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.73636e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.709e+12, 2.73638e+10 } } mol +Time: 1.26e+08 s, dt: 2640000 s, Cycle: 32 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-03 ) ( Rwell ) = ( 1.60e-08 ) ( R ) = ( 1.58e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00153271 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570116 s | Solve Time: 0.330416 s + compositionalMultiphaseFlow: Max pressure change: 12658.569 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.005 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2997173781670313e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-04 ) ( Rwell ) = ( 6.50e-08 ) ( R ) = ( 3.23e-04 ) + Last LinSolve(iter,res) = ( 4, 1.53e-03 ) +wellControls1: BHP (at the specified reference elevation): 4978660.243886277 Pa +wellControls1: Total rate: -979.5821710778366 mol/s; total surface volumetric rate: -23.148148152293388 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148152293388 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.149 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.4973e+06, 1.07887e+07, 1.10552e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.81863e+06, -389957 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.73378e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.10067e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.32371e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.73378e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.70644e+12, 2.7338e+10 } } mol +Time: 1.29e+08 s, dt: 4320000 s, Cycle: 33 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.33e-03 ) ( Rwell ) = ( 6.53e-08 ) ( R ) = ( 2.33e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236836 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572313 s | Solve Time: 0.330063 s + compositionalMultiphaseFlow: Max pressure change: 20698.479 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.596 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.332098825164053e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 1.74e-07 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 2.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00241848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569293 s | Solve Time: 0.330516 s + compositionalMultiphaseFlow: Max pressure change: 8.325 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.097 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.670225534602167e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-06 ) ( Rwell ) = ( 9.17e-11 ) ( R ) = ( 1.17e-06 ) + Last LinSolve(iter,res) = ( 4, 2.42e-03 ) +wellControls1: BHP (at the specified reference elevation): 4948262.720793662 Pa +wellControls1: Total rate: -979.5821705958738 mol/s; total surface volumetric rate: -23.148148147747992 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147747992 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.244 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.4766e+06, 1.07724e+07, 1.10383e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.83129e+06, -399609 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.72955e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.09432e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.32011e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.72955e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.70225e+12, 2.72957e+10 } } mol +Time: 1.33e+08 s, dt: 4320000 s, Cycle: 34 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-03 ) ( Rwell ) = ( 1.91e-10 ) ( R ) = ( 2.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00239217 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.57113 s | Solve Time: 0.330705 s + compositionalMultiphaseFlow: Max pressure change: 20709.199 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.602 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.738540443887217e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 1.75e-07 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00254313 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570427 s | Solve Time: 0.330879 s + compositionalMultiphaseFlow: Max pressure change: 8.039 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7379909167967185e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-06 ) ( Rwell ) = ( 1.12e-10 ) ( R ) = ( 1.28e-06 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) +wellControls1: BHP (at the specified reference elevation): 4917812.611244863 Pa +wellControls1: Total rate: -979.5821719000558 mol/s; total surface volumetric rate: -23.14814814793347 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814793347 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.244 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.45588e+06, 1.0756e+07, 1.10215e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.852e+06, -415410 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.72531e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.08797e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.31652e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.72531e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.69806e+12, 2.72534e+10 } } mol +Time: 1.38e+08 s, dt: 4320000 s, Cycle: 35 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-03 ) ( Rwell ) = ( 2.12e-10 ) ( R ) = ( 2.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235601 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568781 s | Solve Time: 0.33046 s + compositionalMultiphaseFlow: Max pressure change: 20721.888 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.604 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.856881847230653e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 1.78e-07 ) ( R ) = ( 1.30e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00238595 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.57041 s | Solve Time: 0.331476 s + compositionalMultiphaseFlow: Max pressure change: 8.620 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.856746400021649e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-06 ) ( Rwell ) = ( 8.66e-11 ) ( R ) = ( 1.15e-06 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) +wellControls1: BHP (at the specified reference elevation): 4887296.255943198 Pa +wellControls1: Total rate: -979.5821717629018 mol/s; total surface volumetric rate: -23.148148148186618 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148186618 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.43515e+06, 1.07396e+07, 1.10046e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.87271e+06, -431220 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.72108e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.08162e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.31292e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.72108e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.69387e+12, 2.72111e+10 } } mol +Time: 1.42e+08 s, dt: 4320000 s, Cycle: 36 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.52e-03 ) ( Rwell ) = ( 1.88e-10 ) ( R ) = ( 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00254258 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571031 s | Solve Time: 0.330984 s + compositionalMultiphaseFlow: Max pressure change: 20735.987 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.608 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.960757011256533e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 1.80e-07 ) ( R ) = ( 1.33e-03 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00275544 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.574612 s | Solve Time: 0.330882 s + compositionalMultiphaseFlow: Max pressure change: 8.123 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.95921274654043e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-06 ) ( Rwell ) = ( 1.47e-10 ) ( R ) = ( 1.52e-06 ) + Last LinSolve(iter,res) = ( 4, 2.76e-03 ) +wellControls1: BHP (at the specified reference elevation): 4856712.898904027 Pa +wellControls1: Total rate: -979.5821710351845 mol/s; total surface volumetric rate: -23.14814814819829 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814819829 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.246 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.4144e+06, 1.07232e+07, 1.09877e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.89344e+06, -447037 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.71685e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.07527e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.30932e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.71685e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.68968e+12, 2.71688e+10 } } mol +Time: 1.46e+08 s, dt: 4320000 s, Cycle: 37 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-03 ) ( Rwell ) = ( 2.50e-10 ) ( R ) = ( 2.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00254136 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58711 s | Solve Time: 0.330731 s + compositionalMultiphaseFlow: Max pressure change: 20749.936 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.612 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.055297886385034e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-03 ) ( Rwell ) = ( 1.82e-07 ) ( R ) = ( 1.34e-03 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00274103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568005 s | Solve Time: 0.330756 s + compositionalMultiphaseFlow: Max pressure change: 8.182 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.056754254744277e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-06 ) ( Rwell ) = ( 1.46e-10 ) ( R ) = ( 1.51e-06 ) + Last LinSolve(iter,res) = ( 4, 2.74e-03 ) +wellControls1: BHP (at the specified reference elevation): 4826061.57556172 Pa +wellControls1: Total rate: -979.582170255756 mol/s; total surface volumetric rate: -23.14814814821815 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814821815 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.39365e+06, 1.07068e+07, 1.09709e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.91419e+06, -462859 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.71262e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.06893e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.30573e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.71262e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.68549e+12, 2.71265e+10 } } mol +Time: 1.50e+08 s, dt: 4320000 s, Cycle: 38 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-03 ) ( Rwell ) = ( 2.49e-10 ) ( R ) = ( 2.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235713 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568663 s | Solve Time: 0.330373 s + compositionalMultiphaseFlow: Max pressure change: 20763.657 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.616 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.1592261523781815e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-03 ) ( Rwell ) = ( 1.85e-07 ) ( R ) = ( 1.32e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00239166 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.56948 s | Solve Time: 0.330813 s + compositionalMultiphaseFlow: Max pressure change: 8.848 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.1600544564701636e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-06 ) ( Rwell ) = ( 8.81e-11 ) ( R ) = ( 1.16e-06 ) + Last LinSolve(iter,res) = ( 4, 2.39e-03 ) +wellControls1: BHP (at the specified reference elevation): 4795341.305020696 Pa +wellControls1: Total rate: -979.5821695847679 mol/s; total surface volumetric rate: -23.148148148238743 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148238743 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.37287e+06, 1.06904e+07, 1.09541e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.93495e+06, -478687 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.70839e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.06258e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.30213e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.70839e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.6813e+12, 2.70842e+10 } } mol +Time: 1.55e+08 s, dt: 3000000 s, Cycle: 39 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-03 ) ( Rwell ) = ( 1.92e-10 ) ( R ) = ( 1.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00169938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570056 s | Solve Time: 0.33084 s + compositionalMultiphaseFlow: Max pressure change: 14432.402 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.601 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0380219512006192e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-04 ) ( Rwell ) = ( 9.02e-08 ) ( R ) = ( 5.38e-04 ) + Last LinSolve(iter,res) = ( 4, 1.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 4773978.008435329 Pa +wellControls1: Total rate: -979.5821537141984 mol/s; total surface volumetric rate: -23.148148149727902 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148149727902 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.35844e+06, 1.0679e+07, 1.09424e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.95572e+06, -494518 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.70545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.05817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.29963e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.70545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.67839e+12, 2.70547e+10 } } mol +Time: 1.58e+08 s, dt: 4320000 s, Cycle: 40 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.35e-03 ) ( Rwell ) = ( 9.07e-08 ) ( R ) = ( 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00234431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571962 s | Solve Time: 0.330627 s + compositionalMultiphaseFlow: Max pressure change: 20792.238 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.627 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2791244003173006e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 1.89e-07 ) ( R ) = ( 1.33e-03 ) + Last LinSolve(iter,res) = ( 4, 2.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00229426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.576095 s | Solve Time: 0.330835 s + compositionalMultiphaseFlow: Max pressure change: 8.399 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.31621626217904e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-06 ) ( Rwell ) = ( 1.02e-10 ) ( R ) = ( 1.12e-06 ) + Last LinSolve(iter,res) = ( 4, 2.29e-03 ) +wellControls1: BHP (at the specified reference elevation): 4743123.210447031 Pa +wellControls1: Total rate: -979.5821560991412 mol/s; total surface volumetric rate: -23.14814814853664 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814853664 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.33764e+06, 1.06626e+07, 1.09255e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.97015e+06, -505515 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.70122e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.05182e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.29603e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.70122e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.6742e+12, 2.70125e+10 } } mol +Time: 1.62e+08 s, dt: 4320000 s, Cycle: 41 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-03 ) ( Rwell ) = ( 2.07e-10 ) ( R ) = ( 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.002347 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569583 s | Solve Time: 0.330427 s + compositionalMultiphaseFlow: Max pressure change: 20803.756 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.633 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.3972551488913325e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 1.91e-07 ) ( R ) = ( 1.33e-03 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00230966 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571119 s | Solve Time: 0.330732 s + compositionalMultiphaseFlow: Max pressure change: 8.556 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.397639652431451e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-06 ) ( Rwell ) = ( 1.03e-10 ) ( R ) = ( 1.13e-06 ) + Last LinSolve(iter,res) = ( 4, 2.31e-03 ) +wellControls1: BHP (at the specified reference elevation): 4712214.4083415875 Pa +wellControls1: Total rate: -979.5821617663341 mol/s; total surface volumetric rate: -23.148148148400995 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148400995 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.250 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.31683e+06, 1.06462e+07, 1.09087e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.99095e+06, -521351 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.69698e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.04548e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.29244e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.69698e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.67001e+12, 2.69702e+10 } } mol +Time: 1.66e+08 s, dt: 4320000 s, Cycle: 42 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.57e-03 ) ( Rwell ) = ( 2.09e-10 ) ( R ) = ( 2.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573427 s | Solve Time: 0.331978 s + compositionalMultiphaseFlow: Max pressure change: 20819.284 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.636 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5337301024517274e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-03 ) ( Rwell ) = ( 1.94e-07 ) ( R ) = ( 1.37e-03 ) + Last LinSolve(iter,res) = ( 4, 2.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235338 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568963 s | Solve Time: 0.331697 s + compositionalMultiphaseFlow: Max pressure change: 8.879 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5336632892301054e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-06 ) ( Rwell ) = ( 8.01e-11 ) ( R ) = ( 1.11e-06 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) +wellControls1: BHP (at the specified reference elevation): 4681232.230797099 Pa +wellControls1: Total rate: -979.5821644215495 mol/s; total surface volumetric rate: -23.148148147876977 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147876977 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.250 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.296e+06, 1.06298e+07, 1.08919e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.01176e+06, -537190 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.69275e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.03913e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.28884e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.69275e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.66582e+12, 2.69279e+10 } } mol +Time: 1.71e+08 s, dt: 4320000 s, Cycle: 43 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.57e-03 ) ( Rwell ) = ( 1.87e-10 ) ( R ) = ( 2.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00240008 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571278 s | Solve Time: 0.331571 s + compositionalMultiphaseFlow: Max pressure change: 20835.378 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.641 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.6405510989444565e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-03 ) ( Rwell ) = ( 1.96e-07 ) ( R ) = ( 1.36e-03 ) + Last LinSolve(iter,res) = ( 4, 2.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00249516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571908 s | Solve Time: 0.331177 s + compositionalMultiphaseFlow: Max pressure change: 8.723 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.6400205899743696e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-06 ) ( Rwell ) = ( 1.14e-10 ) ( R ) = ( 1.30e-06 ) + Last LinSolve(iter,res) = ( 4, 2.50e-03 ) +wellControls1: BHP (at the specified reference elevation): 4650176.316497895 Pa +wellControls1: Total rate: -979.5821655052191 mol/s; total surface volumetric rate: -23.14814814806234 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814806234 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.27516e+06, 1.06134e+07, 1.0875e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.03259e+06, -553031 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.68852e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.03278e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.28524e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.68852e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.66163e+12, 2.68856e+10 } } mol +Time: 1.75e+08 s, dt: 4320000 s, Cycle: 44 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.58e-03 ) ( Rwell ) = ( 2.22e-10 ) ( R ) = ( 2.58e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00255171 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.57209 s | Solve Time: 0.331676 s + compositionalMultiphaseFlow: Max pressure change: 20851.426 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.644 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.7599459040981174e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-03 ) ( Rwell ) = ( 1.99e-07 ) ( R ) = ( 1.41e-03 ) + Last LinSolve(iter,res) = ( 4, 2.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00267461 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.576076 s | Solve Time: 0.331619 s + compositionalMultiphaseFlow: Max pressure change: 8.764 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.7585033358110707e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-06 ) ( Rwell ) = ( 1.41e-10 ) ( R ) = ( 1.48e-06 ) + Last LinSolve(iter,res) = ( 4, 2.67e-03 ) +wellControls1: BHP (at the specified reference elevation): 4619046.09588719 Pa +wellControls1: Total rate: -979.5821658861805 mol/s; total surface volumetric rate: -23.148148148303736 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148303736 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.252 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.25429e+06, 1.0597e+07, 1.08582e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.05344e+06, -568873 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.68429e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.02643e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.28165e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.68429e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.65745e+12, 2.68433e+10 } } mol +Time: 1.79e+08 s, dt: 4320000 s, Cycle: 45 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.59e-03 ) ( Rwell ) = ( 2.50e-10 ) ( R ) = ( 2.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00244733 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572943 s | Solve Time: 0.331963 s + compositionalMultiphaseFlow: Max pressure change: 20867.902 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.648 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.8758341475441114e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-03 ) ( Rwell ) = ( 2.02e-07 ) ( R ) = ( 1.38e-03 ) + Last LinSolve(iter,res) = ( 4, 2.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00251613 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.575272 s | Solve Time: 0.331957 s + compositionalMultiphaseFlow: Max pressure change: 8.560 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.8785857353905726e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-06 ) ( Rwell ) = ( 9.97e-11 ) ( R ) = ( 1.15e-06 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) +wellControls1: BHP (at the specified reference elevation): 4587840.863329087 Pa +wellControls1: Total rate: -979.5821659588797 mol/s; total surface volumetric rate: -23.148148147603894 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147603894 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.23342e+06, 1.05807e+07, 1.08414e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.0743e+06, -584717 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.68006e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.02008e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.27805e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.68006e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.65326e+12, 2.6801e+10 } } mol +Time: 1.84e+08 s, dt: 4320000 s, Cycle: 46 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.60e-03 ) ( Rwell ) = ( 2.10e-10 ) ( R ) = ( 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0023602 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.574189 s | Solve Time: 0.33141 s + compositionalMultiphaseFlow: Max pressure change: 20883.666 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.653 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.988949076079052e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-03 ) ( Rwell ) = ( 2.04e-07 ) ( R ) = ( 1.39e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00233076 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568393 s | Solve Time: 0.331427 s + compositionalMultiphaseFlow: Max pressure change: 9.258 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.987596702310526e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-06 ) ( Rwell ) = ( 8.44e-11 ) ( R ) = ( 1.14e-06 ) + Last LinSolve(iter,res) = ( 4, 2.33e-03 ) +wellControls1: BHP (at the specified reference elevation): 4556559.87033746 Pa +wellControls1: Total rate: -979.5821659864374 mol/s; total surface volumetric rate: -23.148148148328826 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148328826 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.21253e+06, 1.05643e+07, 1.08246e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.09517e+06, -600561 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.67582e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.01374e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.27445e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.67582e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.64907e+12, 2.67587e+10 } } mol +Time: 1.88e+08 s, dt: 1320000 s, Cycle: 47 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.97e-04 ) ( Rwell ) = ( 1.95e-10 ) ( R ) = ( 7.97e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00665388 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570148 s | Solve Time: 0.252297 s + compositionalMultiphaseFlow: Max pressure change: 6373.814 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.078 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.601293707689024e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-04 ) ( Rwell ) = ( 1.92e-08 ) ( R ) = ( 4.86e-04 ) + Last LinSolve(iter,res) = ( 3, 6.65e-03 ) +wellControls1: BHP (at the specified reference elevation): 4547017.935244296 Pa +wellControls1: Total rate: -979.582217547441 mol/s; total surface volumetric rate: -23.148148145217444 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148145217444 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.20615e+06, 1.05593e+07, 1.08194e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.11606e+06, -616406 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.67453e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.0118e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.27335e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.67453e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.64779e+12, 2.67458e+10 } } mol +Time: 1.89e+08 s, dt: 2640000 s, Cycle: 48 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.65e-03 ) ( Rwell ) = ( 1.94e-08 ) ( R ) = ( 1.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00166648 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570979 s | Solve Time: 0.332447 s + compositionalMultiphaseFlow: Max pressure change: 12789.873 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.046 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7452995604294586e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-04 ) ( Rwell ) = ( 7.86e-08 ) ( R ) = ( 3.42e-04 ) + Last LinSolve(iter,res) = ( 4, 1.67e-03 ) +wellControls1: BHP (at the specified reference elevation): 4527832.121551093 Pa +wellControls1: Total rate: -979.5821651420814 mol/s; total surface volumetric rate: -23.14814815320047 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814815320047 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.156 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.19336e+06, 1.05492e+07, 1.08091e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.12244e+06, -621247 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.67195e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.00792e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.27115e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.67195e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.64523e+12, 2.672e+10 } } mol +Time: 1.92e+08 s, dt: 4320000 s, Cycle: 49 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 7.91e-08 ) ( R ) = ( 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00255297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570053 s | Solve Time: 0.331223 s + compositionalMultiphaseFlow: Max pressure change: 20918.807 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.664 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.115680968779344e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-03 ) ( Rwell ) = ( 2.10e-07 ) ( R ) = ( 1.47e-03 ) + Last LinSolve(iter,res) = ( 4, 2.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00258493 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567862 s | Solve Time: 0.331616 s + compositionalMultiphaseFlow: Max pressure change: 8.663 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.102 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.1920129751081845e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-06 ) ( Rwell ) = ( 1.16e-10 ) ( R ) = ( 1.38e-06 ) + Last LinSolve(iter,res) = ( 4, 2.58e-03 ) +wellControls1: BHP (at the specified reference elevation): 4496390.385749549 Pa +wellControls1: Total rate: -979.5821654013587 mol/s; total surface volumetric rate: -23.1481481485915 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.1481481485915 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.255 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.17243e+06, 1.05329e+07, 1.07923e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.13523e+06, -630929 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66771e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 4.00157e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26756e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66771e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.64104e+12, 2.66777e+10 } } mol +Time: 1.96e+08 s, dt: 4320000 s, Cycle: 50 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.63e-03 ) ( Rwell ) = ( 2.29e-10 ) ( R ) = ( 2.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568692 s | Solve Time: 0.331645 s + compositionalMultiphaseFlow: Max pressure change: 20932.552 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.670 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.304705341657723e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-03 ) ( Rwell ) = ( 2.13e-07 ) ( R ) = ( 1.42e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00225573 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570379 s | Solve Time: 0.331484 s + compositionalMultiphaseFlow: Max pressure change: 9.215 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.307670636334194e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-06 ) ( Rwell ) = ( 9.97e-11 ) ( R ) = ( 1.13e-06 ) + Last LinSolve(iter,res) = ( 4, 2.26e-03 ) +wellControls1: BHP (at the specified reference elevation): 4464884.478871564 Pa +wellControls1: Total rate: -979.5821665973084 mol/s; total surface volumetric rate: -23.148148147827687 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147827687 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.256 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.15149e+06, 1.05165e+07, 1.07755e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.15616e+06, -646776 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66348e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99522e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26396e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66348e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.63685e+12, 2.66354e+10 } } mol +Time: 2.01e+08 s, dt: 4320000 s, Cycle: 51 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.63e-03 ) ( Rwell ) = ( 2.14e-10 ) ( R ) = ( 2.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00253725 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569998 s | Solve Time: 0.331546 s + compositionalMultiphaseFlow: Max pressure change: 20950.111 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.674 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.432861960308344e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-03 ) ( Rwell ) = ( 2.16e-07 ) ( R ) = ( 1.48e-03 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00257355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571819 s | Solve Time: 0.331506 s + compositionalMultiphaseFlow: Max pressure change: 8.977 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.101 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.4322088494096477e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-06 ) ( Rwell ) = ( 1.16e-10 ) ( R ) = ( 1.36e-06 ) + Last LinSolve(iter,res) = ( 4, 2.57e-03 ) +wellControls1: BHP (at the specified reference elevation): 4433299.236054566 Pa +wellControls1: Total rate: -979.582166353331 mol/s; total surface volumetric rate: -23.14814814807465 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814807465 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.257 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.13053e+06, 1.05001e+07, 1.07587e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.1771e+06, -662622 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65925e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.98888e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26036e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65925e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.63266e+12, 2.65931e+10 } } mol +Time: 2.05e+08 s, dt: 4320000 s, Cycle: 52 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-03 ) ( Rwell ) = ( 2.32e-10 ) ( R ) = ( 2.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0023637 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570794 s | Solve Time: 0.332172 s + compositionalMultiphaseFlow: Max pressure change: 20967.054 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.679 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.545544445872963e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 2.19e-07 ) ( R ) = ( 1.44e-03 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00223428 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567338 s | Solve Time: 0.331928 s + compositionalMultiphaseFlow: Max pressure change: 9.398 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.5442595514598736e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-06 ) ( Rwell ) = ( 9.78e-11 ) ( R ) = ( 1.12e-06 ) + Last LinSolve(iter,res) = ( 4, 2.23e-03 ) +wellControls1: BHP (at the specified reference elevation): 4401634.212087513 Pa +wellControls1: Total rate: -979.582165626824 mol/s; total surface volumetric rate: -23.148148148082115 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148082115 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.10956e+06, 1.04837e+07, 1.07419e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.19806e+06, -678467 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65502e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.98253e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25677e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65502e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.62847e+12, 2.65508e+10 } } mol +Time: 2.09e+08 s, dt: 4320000 s, Cycle: 53 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.65e-03 ) ( Rwell ) = ( 2.14e-10 ) ( R ) = ( 2.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00253869 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568407 s | Solve Time: 0.331295 s + compositionalMultiphaseFlow: Max pressure change: 20984.742 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.684 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.663442481651515e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-03 ) ( Rwell ) = ( 2.22e-07 ) ( R ) = ( 1.50e-03 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00247882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570103 s | Solve Time: 0.331783 s + compositionalMultiphaseFlow: Max pressure change: 9.166 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.101 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.663182711668213e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-06 ) ( Rwell ) = ( 1.06e-10 ) ( R ) = ( 1.26e-06 ) + Last LinSolve(iter,res) = ( 4, 2.48e-03 ) +wellControls1: BHP (at the specified reference elevation): 4369888.79935645 Pa +wellControls1: Total rate: -979.5821648604106 mol/s; total surface volumetric rate: -23.14814814834269 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814834269 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.08856e+06, 1.04673e+07, 1.07251e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.21903e+06, -694313 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65079e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.97618e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25317e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65079e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.62428e+12, 2.65085e+10 } } mol +Time: 2.14e+08 s, dt: 4320000 s, Cycle: 54 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.66e-03 ) ( Rwell ) = ( 2.24e-10 ) ( R ) = ( 2.66e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00230031 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567899 s | Solve Time: 0.332581 s + compositionalMultiphaseFlow: Max pressure change: 21001.576 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.690 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.776739708807099e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 2.25e-07 ) ( R ) = ( 1.44e-03 ) + Last LinSolve(iter,res) = ( 4, 2.30e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00227299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569865 s | Solve Time: 0.331414 s + compositionalMultiphaseFlow: Max pressure change: 9.946 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.092 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.7781421314295756e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-06 ) ( Rwell ) = ( 9.30e-11 ) ( R ) = ( 1.05e-06 ) + Last LinSolve(iter,res) = ( 4, 2.27e-03 ) +wellControls1: BHP (at the specified reference elevation): 4338062.224346974 Pa +wellControls1: Total rate: -979.5821641783294 mol/s; total surface volumetric rate: -23.148148147873293 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147873293 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.260 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.06755e+06, 1.04509e+07, 1.07083e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.24003e+06, -710158 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64655e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.96983e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24957e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64655e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.62009e+12, 2.64662e+10 } } mol +Time: 2.18e+08 s, dt: 3000000 s, Cycle: 55 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-03 ) ( Rwell ) = ( 2.11e-10 ) ( R ) = ( 1.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00168598 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569525 s | Solve Time: 0.332493 s + compositionalMultiphaseFlow: Max pressure change: 14599.810 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.650 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.837701051916497e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.55e-04 ) ( Rwell ) = ( 1.10e-07 ) ( R ) = ( 5.55e-04 ) + Last LinSolve(iter,res) = ( 4, 1.69e-03 ) +wellControls1: BHP (at the specified reference elevation): 4315925.419003899 Pa +wellControls1: Total rate: -979.5821452599959 mol/s; total surface volumetric rate: -23.148148150415153 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148150415153 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.05295e+06, 1.04396e+07, 1.06966e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.26104e+06, -726003 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64362e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.96542e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24707e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64362e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.61718e+12, 2.64368e+10 } } mol +Time: 2.21e+08 s, dt: 4320000 s, Cycle: 56 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 1.11e-07 ) ( R ) = ( 2.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570624 s | Solve Time: 0.331334 s + compositionalMultiphaseFlow: Max pressure change: 21035.570 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.703 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.110828372676622e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-03 ) ( Rwell ) = ( 2.31e-07 ) ( R ) = ( 1.53e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00247282 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570571 s | Solve Time: 0.332058 s + compositionalMultiphaseFlow: Max pressure change: 9.408 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.947004944051315e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-06 ) ( Rwell ) = ( 1.01e-10 ) ( R ) = ( 1.29e-06 ) + Last LinSolve(iter,res) = ( 4, 2.47e-03 ) +wellControls1: BHP (at the specified reference elevation): 4283942.204148832 Pa +wellControls1: Total rate: -979.5821503745965 mol/s; total surface volumetric rate: -23.148148147962488 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147962488 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.261 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.03191e+06, 1.04232e+07, 1.06798e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.27564e+06, -737006 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63938e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.95908e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24348e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63938e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.61299e+12, 2.63945e+10 } } mol +Time: 2.25e+08 s, dt: 4320000 s, Cycle: 57 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-03 ) ( Rwell ) = ( 2.21e-10 ) ( R ) = ( 2.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00251618 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.573807 s | Solve Time: 0.331035 s + compositionalMultiphaseFlow: Max pressure change: 21049.469 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.708 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.066155888717617e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-03 ) ( Rwell ) = ( 2.34e-07 ) ( R ) = ( 1.54e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00242946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569669 s | Solve Time: 0.330814 s + compositionalMultiphaseFlow: Max pressure change: 9.590 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.067230196027396e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-06 ) ( Rwell ) = ( 9.49e-11 ) ( R ) = ( 1.25e-06 ) + Last LinSolve(iter,res) = ( 4, 2.43e-03 ) +wellControls1: BHP (at the specified reference elevation): 4251895.083107691 Pa +wellControls1: Total rate: -979.5821565053648 mol/s; total surface volumetric rate: -23.148148147821413 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147821413 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.01085e+06, 1.04068e+07, 1.0663e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.29668e+06, -752850 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63515e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.95273e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23988e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63515e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.6088e+12, 2.63522e+10 } } mol +Time: 2.30e+08 s, dt: 4320000 s, Cycle: 58 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.70e-03 ) ( Rwell ) = ( 2.17e-10 ) ( R ) = ( 2.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00256312 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569108 s | Solve Time: 0.331264 s + compositionalMultiphaseFlow: Max pressure change: 21067.779 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.713 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.200042479420631e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ( Rwell ) = ( 2.37e-07 ) ( R ) = ( 1.55e-03 ) + Last LinSolve(iter,res) = ( 4, 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00258939 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569623 s | Solve Time: 0.331401 s + compositionalMultiphaseFlow: Max pressure change: 9.746 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.199810498319636e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-06 ) ( Rwell ) = ( 1.38e-10 ) ( R ) = ( 1.46e-06 ) + Last LinSolve(iter,res) = ( 4, 2.59e-03 ) +wellControls1: BHP (at the specified reference elevation): 4219762.810654903 Pa +wellControls1: Total rate: -979.5821593585079 mol/s; total surface volumetric rate: -23.148148147743747 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147743747 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.263 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.98977e+06, 1.03904e+07, 1.06462e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.31774e+06, -768693 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63092e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.94638e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23628e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63092e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.60461e+12, 2.63099e+10 } } mol +Time: 2.34e+08 s, dt: 4320000 s, Cycle: 59 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.71e-03 ) ( Rwell ) = ( 2.61e-10 ) ( R ) = ( 2.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00248137 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572874 s | Solve Time: 0.331184 s + compositionalMultiphaseFlow: Max pressure change: 21086.447 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.715 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.345312641986567e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ( Rwell ) = ( 2.41e-07 ) ( R ) = ( 1.55e-03 ) + Last LinSolve(iter,res) = ( 4, 2.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00234114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569444 s | Solve Time: 0.333477 s + compositionalMultiphaseFlow: Max pressure change: 9.527 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.098 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.345510383809483e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-06 ) ( Rwell ) = ( 9.56e-11 ) ( R ) = ( 1.22e-06 ) + Last LinSolve(iter,res) = ( 4, 2.34e-03 ) +wellControls1: BHP (at the specified reference elevation): 4187545.084487327 Pa +wellControls1: Total rate: -979.5821606181589 mol/s; total surface volumetric rate: -23.148148147981672 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147981672 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.264 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.96867e+06, 1.0374e+07, 1.06293e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.33882e+06, -784537 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62669e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.94003e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23269e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62669e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.60042e+12, 2.62676e+10 } } mol +Time: 2.38e+08 s, dt: 4320000 s, Cycle: 60 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-03 ) ( Rwell ) = ( 2.20e-10 ) ( R ) = ( 2.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00255925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572577 s | Solve Time: 0.330839 s + compositionalMultiphaseFlow: Max pressure change: 21104.582 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.722 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.47098158390591e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-03 ) ( Rwell ) = ( 2.44e-07 ) ( R ) = ( 1.57e-03 ) + Last LinSolve(iter,res) = ( 4, 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00267597 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572287 s | Solve Time: 0.332131 s + compositionalMultiphaseFlow: Max pressure change: 9.896 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.468601143616581e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-06 ) ( Rwell ) = ( 1.40e-10 ) ( R ) = ( 1.53e-06 ) + Last LinSolve(iter,res) = ( 4, 2.68e-03 ) +wellControls1: BHP (at the specified reference elevation): 4155241.3708367427 Pa +wellControls1: Total rate: -979.5821610800992 mol/s; total surface volumetric rate: -23.14814814817463 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814817463 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.94756e+06, 1.03576e+07, 1.06125e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.35992e+06, -800379 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62246e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.93369e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22909e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62246e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.59623e+12, 2.62254e+10 } } mol +Time: 2.43e+08 s, dt: 4320000 s, Cycle: 61 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-03 ) ( Rwell ) = ( 2.66e-10 ) ( R ) = ( 2.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00256021 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569086 s | Solve Time: 0.331307 s + compositionalMultiphaseFlow: Max pressure change: 21123.064 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.727 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.588722256672952e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-03 ) ( Rwell ) = ( 2.48e-07 ) ( R ) = ( 1.58e-03 ) + Last LinSolve(iter,res) = ( 4, 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00254885 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571172 s | Solve Time: 0.331441 s + compositionalMultiphaseFlow: Max pressure change: 10.018 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.590185019916817e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-06 ) ( Rwell ) = ( 1.35e-10 ) ( R ) = ( 1.44e-06 ) + Last LinSolve(iter,res) = ( 4, 2.55e-03 ) +wellControls1: BHP (at the specified reference elevation): 4122850.9765034574 Pa +wellControls1: Total rate: -979.5821612772727 mol/s; total surface volumetric rate: -23.148148148636466 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148636466 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.92643e+06, 1.03413e+07, 1.05957e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.38103e+06, -816221 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61823e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.92734e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22549e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61823e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.59204e+12, 2.61831e+10 } } mol +Time: 2.47e+08 s, dt: 4320000 s, Cycle: 62 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-03 ) ( Rwell ) = ( 2.62e-10 ) ( R ) = ( 2.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00255809 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567182 s | Solve Time: 0.332165 s + compositionalMultiphaseFlow: Max pressure change: 21141.711 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.733 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.713246580858367e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-03 ) ( Rwell ) = ( 2.52e-07 ) ( R ) = ( 1.60e-03 ) + Last LinSolve(iter,res) = ( 4, 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00253382 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.566667 s | Solve Time: 0.331537 s + compositionalMultiphaseFlow: Max pressure change: 10.097 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.711299826989148e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-06 ) ( Rwell ) = ( 1.35e-10 ) ( R ) = ( 1.45e-06 ) + Last LinSolve(iter,res) = ( 4, 2.53e-03 ) +wellControls1: BHP (at the specified reference elevation): 4090373.1282314914 Pa +wellControls1: Total rate: -979.5821613217246 mol/s; total surface volumetric rate: -23.148148147931632 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147931632 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.90527e+06, 1.03249e+07, 1.05789e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.40216e+06, -832062 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61399e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.92099e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22189e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61399e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.58785e+12, 2.61408e+10 } } mol +Time: 2.51e+08 s, dt: 1320000 s, Cycle: 63 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.39e-04 ) ( Rwell ) = ( 2.63e-10 ) ( R ) = ( 8.39e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00660795 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568974 s | Solve Time: 0.252593 s + compositionalMultiphaseFlow: Max pressure change: 6453.554 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.924091911995276e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-04 ) ( Rwell ) = ( 2.37e-08 ) ( R ) = ( 4.94e-04 ) + Last LinSolve(iter,res) = ( 3, 6.61e-03 ) +wellControls1: BHP (at the specified reference elevation): 4080463.3399813343 Pa +wellControls1: Total rate: -979.5822123650528 mol/s; total surface volumetric rate: -23.14814814592489 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814592489 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.89882e+06, 1.03199e+07, 1.05738e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.42332e+06, -847903 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.6127e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.91905e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2208e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.6127e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.58657e+12, 2.61279e+10 } } mol +Time: 2.52e+08 s, dt: 2640000 s, Cycle: 64 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-03 ) ( Rwell ) = ( 2.39e-08 ) ( R ) = ( 1.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00152935 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570093 s | Solve Time: 0.331033 s + compositionalMultiphaseFlow: Max pressure change: 12949.621 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.255143893847844e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.15e-04 ) ( Rwell ) = ( 9.73e-08 ) ( R ) = ( 4.15e-04 ) + Last LinSolve(iter,res) = ( 4, 1.53e-03 ) +wellControls1: BHP (at the specified reference elevation): 4060538.807259637 Pa +wellControls1: Total rate: -979.5821584773923 mol/s; total surface volumetric rate: -23.148148153981708 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148153981708 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.88587e+06, 1.03099e+07, 1.05635e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.42977e+06, -852742 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61011e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.91517e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2186e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61011e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.58401e+12, 2.6102e+10 } } mol +Time: 2.55e+08 s, dt: 4320000 s, Cycle: 65 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-03 ) ( Rwell ) = ( 9.79e-08 ) ( R ) = ( 2.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0025419 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569993 s | Solve Time: 0.331316 s + compositionalMultiphaseFlow: Max pressure change: 21181.167 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.744 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.2265689503828696e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-03 ) ( Rwell ) = ( 2.59e-07 ) ( R ) = ( 1.61e-03 ) + Last LinSolve(iter,res) = ( 4, 2.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252546 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570635 s | Solve Time: 0.330645 s + compositionalMultiphaseFlow: Max pressure change: 9.454 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.101 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.973919719488464e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-06 ) ( Rwell ) = ( 1.25e-10 ) ( R ) = ( 1.41e-06 ) + Last LinSolve(iter,res) = ( 4, 2.53e-03 ) +wellControls1: BHP (at the specified reference elevation): 4027875.9353545285 Pa +wellControls1: Total rate: -979.582158282477 mol/s; total surface volumetric rate: -23.14814814827404 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814827404 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.86468e+06, 1.02935e+07, 1.05467e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.44272e+06, -862422 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60588e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.90882e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.215e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60588e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.57982e+12, 2.60598e+10 } } mol +Time: 2.59e+08 s, dt: 4320000 s, Cycle: 66 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.76e-03 ) ( Rwell ) = ( 2.56e-10 ) ( R ) = ( 2.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00256614 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.576012 s | Solve Time: 0.330978 s + compositionalMultiphaseFlow: Max pressure change: 21196.630 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.751 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.078448283071026e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-03 ) ( Rwell ) = ( 2.63e-07 ) ( R ) = ( 1.63e-03 ) + Last LinSolve(iter,res) = ( 4, 2.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00251027 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578476 s | Solve Time: 0.331541 s + compositionalMultiphaseFlow: Max pressure change: 10.353 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.080933728254024e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-06 ) ( Rwell ) = ( 1.35e-10 ) ( R ) = ( 1.45e-06 ) + Last LinSolve(iter,res) = ( 4, 2.51e-03 ) +wellControls1: BHP (at the specified reference elevation): 3995138.852517514 Pa +wellControls1: Total rate: -979.5821599952991 mol/s; total surface volumetric rate: -23.148148147727383 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147727383 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.270 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.84347e+06, 1.02771e+07, 1.05299e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.46391e+06, -878261 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60165e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.90248e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2114e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60165e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.57563e+12, 2.60175e+10 } } mol +Time: 2.64e+08 s, dt: 4320000 s, Cycle: 67 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.77e-03 ) ( Rwell ) = ( 2.68e-10 ) ( R ) = ( 2.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00256893 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571131 s | Solve Time: 0.331338 s + compositionalMultiphaseFlow: Max pressure change: 21215.964 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.756 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.234247867415888e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-03 ) ( Rwell ) = ( 2.67e-07 ) ( R ) = ( 1.65e-03 ) + Last LinSolve(iter,res) = ( 4, 2.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00250877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567429 s | Solve Time: 0.331779 s + compositionalMultiphaseFlow: Max pressure change: 10.494 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.232783527655329e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-06 ) ( Rwell ) = ( 1.32e-10 ) ( R ) = ( 1.44e-06 ) + Last LinSolve(iter,res) = ( 4, 2.51e-03 ) +wellControls1: BHP (at the specified reference elevation): 3962310.391790188 Pa +wellControls1: Total rate: -979.5821601218438 mol/s; total surface volumetric rate: -23.148148147955304 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147955304 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.271 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.82225e+06, 1.02607e+07, 1.05131e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.48512e+06, -894100 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59742e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.89613e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20781e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59742e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.57144e+12, 2.59752e+10 } } mol +Time: 2.68e+08 s, dt: 4320000 s, Cycle: 68 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.78e-03 ) ( Rwell ) = ( 2.66e-10 ) ( R ) = ( 2.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252295 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569009 s | Solve Time: 0.331319 s + compositionalMultiphaseFlow: Max pressure change: 21235.364 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.760 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.382619315876582e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ( Rwell ) = ( 2.71e-07 ) ( R ) = ( 1.66e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236461 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.570549 s | Solve Time: 0.330972 s + compositionalMultiphaseFlow: Max pressure change: 10.564 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.383164235541528e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-06 ) ( Rwell ) = ( 9.08e-11 ) ( R ) = ( 1.27e-06 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) +wellControls1: BHP (at the specified reference elevation): 3929390.0671822573 Pa +wellControls1: Total rate: -979.5821597168102 mol/s; total surface volumetric rate: -23.14814814849907 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814849907 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.272 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.801e+06, 1.02443e+07, 1.04963e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.50634e+06, -909938 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59319e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.88978e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20421e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59319e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.56725e+12, 2.59329e+10 } } mol +Time: 2.72e+08 s, dt: 4320000 s, Cycle: 69 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.79e-03 ) ( Rwell ) = ( 2.26e-10 ) ( R ) = ( 2.79e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567888 s | Solve Time: 0.33183 s + compositionalMultiphaseFlow: Max pressure change: 21254.822 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.766 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.520586497999915e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ( Rwell ) = ( 2.76e-07 ) ( R ) = ( 1.68e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00232516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568849 s | Solve Time: 0.331784 s + compositionalMultiphaseFlow: Max pressure change: 10.662 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.521019951273189e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-06 ) ( Rwell ) = ( 8.78e-11 ) ( R ) = ( 1.25e-06 ) + Last LinSolve(iter,res) = ( 4, 2.33e-03 ) +wellControls1: BHP (at the specified reference elevation): 3896377.1536678234 Pa +wellControls1: Total rate: -979.5821591890029 mol/s; total surface volumetric rate: -23.14814814851334 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814851334 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.273 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.77974e+06, 1.0228e+07, 1.04795e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.52759e+06, -925775 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.58896e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.88343e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20061e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.58896e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.56306e+12, 2.58906e+10 } } mol +Time: 2.77e+08 s, dt: 4320000 s, Cycle: 70 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.80e-03 ) ( Rwell ) = ( 2.24e-10 ) ( R ) = ( 2.80e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252389 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.571028 s | Solve Time: 0.330432 s + compositionalMultiphaseFlow: Max pressure change: 21274.397 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.772 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.658864653592445e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-03 ) ( Rwell ) = ( 2.80e-07 ) ( R ) = ( 1.69e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00236139 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569015 s | Solve Time: 0.332144 s + compositionalMultiphaseFlow: Max pressure change: 10.771 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.65682073300411e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-06 ) ( Rwell ) = ( 9.19e-11 ) ( R ) = ( 1.28e-06 ) + Last LinSolve(iter,res) = ( 4, 2.36e-03 ) +wellControls1: BHP (at the specified reference elevation): 3863270.793625378 Pa +wellControls1: Total rate: -979.5821587233605 mol/s; total surface volumetric rate: -23.148148148019047 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148019047 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.274 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.75845e+06, 1.02116e+07, 1.04627e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.54885e+06, -941611 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.58472e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.87709e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19702e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.58472e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.55888e+12, 2.58483e+10 } } mol +Time: 2.81e+08 s, dt: 3000000 s, Cycle: 71 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-03 ) ( Rwell ) = ( 2.30e-10 ) ( R ) = ( 1.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00165729 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.56635 s | Solve Time: 0.331521 s + compositionalMultiphaseFlow: Max pressure change: 14790.597 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.708 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.743374521469889e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-04 ) ( Rwell ) = ( 1.37e-07 ) ( R ) = ( 6.21e-04 ) + Last LinSolve(iter,res) = ( 4, 1.66e-03 ) +wellControls1: BHP (at the specified reference elevation): 3840240.691398817 Pa +wellControls1: Total rate: -979.5821386414483 mol/s; total surface volumetric rate: -23.14814815106055 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814815106055 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.191 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.74366e+06, 1.02002e+07, 1.0451e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.57014e+06, -957447 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.58178e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.87268e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19452e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.58178e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.55597e+12, 2.58189e+10 } } mol +Time: 2.84e+08 s, dt: 4320000 s, Cycle: 72 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-03 ) ( Rwell ) = ( 1.38e-07 ) ( R ) = ( 2.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00253245 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569699 s | Solve Time: 0.332219 s + compositionalMultiphaseFlow: Max pressure change: 21311.852 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.788 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.0862943140318464e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ( Rwell ) = ( 2.88e-07 ) ( R ) = ( 1.72e-03 ) + Last LinSolve(iter,res) = ( 4, 2.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00228839 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.566735 s | Solve Time: 0.331171 s + compositionalMultiphaseFlow: Max pressure change: 10.821 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.831174608785574e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-06 ) ( Rwell ) = ( 8.68e-11 ) ( R ) = ( 1.26e-06 ) + Last LinSolve(iter,res) = ( 4, 2.29e-03 ) +wellControls1: BHP (at the specified reference elevation): 3806953.6183943935 Pa +wellControls1: Total rate: -979.5821446331721 mol/s; total surface volumetric rate: -23.14814814808243 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814808243 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.275 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.72234e+06, 1.01838e+07, 1.04342e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.58493e+06, -968443 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57755e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.86633e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19092e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57755e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.55178e+12, 2.57766e+10 } } mol +Time: 2.88e+08 s, dt: 4320000 s, Cycle: 73 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.83e-03 ) ( Rwell ) = ( 2.28e-10 ) ( R ) = ( 2.83e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252352 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.566496 s | Solve Time: 0.331183 s + compositionalMultiphaseFlow: Max pressure change: 21327.255 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.793 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.96896789667656e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-03 ) ( Rwell ) = ( 2.92e-07 ) ( R ) = ( 1.73e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00223921 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5681 s | Solve Time: 0.33155 s + compositionalMultiphaseFlow: Max pressure change: 11.043 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.96892463128529e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-06 ) ( Rwell ) = ( 7.91e-11 ) ( R ) = ( 1.16e-06 ) + Last LinSolve(iter,res) = ( 4, 2.24e-03 ) +wellControls1: BHP (at the specified reference elevation): 3773592.944105365 Pa +wellControls1: Total rate: -979.5821512256961 mol/s; total surface volumetric rate: -23.14814814818376 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814818376 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.276 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.701e+06, 1.01674e+07, 1.04174e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.60625e+06, -984278 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57332e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.85998e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18732e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57332e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.54759e+12, 2.57343e+10 } } mol +Time: 2.93e+08 s, dt: 4320000 s, Cycle: 74 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.84e-03 ) ( Rwell ) = ( 2.21e-10 ) ( R ) = ( 2.84e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252292 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569041 s | Solve Time: 0.331098 s + compositionalMultiphaseFlow: Max pressure change: 21347.687 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.797 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.134598750153543e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-03 ) ( Rwell ) = ( 2.97e-07 ) ( R ) = ( 1.74e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00227722 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.572779 s | Solve Time: 0.330712 s + compositionalMultiphaseFlow: Max pressure change: 11.158 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.13429474888494e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-06 ) ( Rwell ) = ( 8.58e-11 ) ( R ) = ( 1.25e-06 ) + Last LinSolve(iter,res) = ( 4, 2.28e-03 ) +wellControls1: BHP (at the specified reference elevation): 3740134.2865344943 Pa +wellControls1: Total rate: -979.5821543795392 mol/s; total surface volumetric rate: -23.148148148109446 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148109446 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.277 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.67964e+06, 1.01511e+07, 1.04006e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.62759e+06, -1.00011e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56909e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.85363e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18373e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56909e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.5434e+12, 2.56921e+10 } } mol +Time: 2.97e+08 s, dt: 4320000 s, Cycle: 75 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.85e-03 ) ( Rwell ) = ( 2.30e-10 ) ( R ) = ( 2.85e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00252335 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569138 s | Solve Time: 0.331341 s + compositionalMultiphaseFlow: Max pressure change: 21368.111 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.801 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.2996850947481e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-03 ) ( Rwell ) = ( 3.02e-07 ) ( R ) = ( 1.75e-03 ) + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00226627 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568946 s | Solve Time: 0.33127 s + compositionalMultiphaseFlow: Max pressure change: 11.262 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.30024103892768e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-06 ) ( Rwell ) = ( 8.51e-11 ) ( R ) = ( 1.25e-06 ) + Last LinSolve(iter,res) = ( 4, 2.27e-03 ) +wellControls1: BHP (at the specified reference elevation): 3706577.216197883 Pa +wellControls1: Total rate: -979.5821558113743 mol/s; total surface volumetric rate: -23.148148148082107 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148082107 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.278 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.65826e+06, 1.01347e+07, 1.03838e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.64895e+06, -1.01594e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56486e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.84729e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18013e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56486e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.53921e+12, 2.56498e+10 } } mol +Time: 3.01e+08 s, dt: 4320000 s, Cycle: 76 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-03 ) ( Rwell ) = ( 2.31e-10 ) ( R ) = ( 2.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235398 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569008 s | Solve Time: 0.331647 s + compositionalMultiphaseFlow: Max pressure change: 21388.398 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.808 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.429885078875543e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-03 ) ( Rwell ) = ( 3.07e-07 ) ( R ) = ( 1.74e-03 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00194303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569839 s | Solve Time: 0.331559 s + compositionalMultiphaseFlow: Max pressure change: 11.566 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.430559328420628e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-06 ) ( Rwell ) = ( 4.93e-11 ) ( R ) = ( 1.06e-06 ) + Last LinSolve(iter,res) = ( 4, 1.94e-03 ) +wellControls1: BHP (at the specified reference elevation): 3672921.0438736947 Pa +wellControls1: Total rate: -979.5821564699713 mol/s; total surface volumetric rate: -23.14814814779661 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814779661 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.279 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.63686e+06, 1.01183e+07, 1.0367e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.67033e+06, -1.03178e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56063e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.84094e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17653e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56063e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.53502e+12, 2.56075e+10 } } mol +Time: 3.06e+08 s, dt: 4320000 s, Cycle: 77 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.88e-03 ) ( Rwell ) = ( 1.97e-10 ) ( R ) = ( 2.88e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00235448 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568077 s | Solve Time: 0.331395 s + compositionalMultiphaseFlow: Max pressure change: 21408.980 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.814 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.574772880631798e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-03 ) ( Rwell ) = ( 3.12e-07 ) ( R ) = ( 1.76e-03 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00192918 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568277 s | Solve Time: 0.331399 s + compositionalMultiphaseFlow: Max pressure change: 11.682 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.575769216978557e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-06 ) ( Rwell ) = ( 4.89e-11 ) ( R ) = ( 1.05e-06 ) + Last LinSolve(iter,res) = ( 4, 1.93e-03 ) +wellControls1: BHP (at the specified reference elevation): 3639164.923317053 Pa +wellControls1: Total rate: -979.5821568186503 mol/s; total surface volumetric rate: -23.14814814802785 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814802785 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.280 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.61544e+06, 1.01019e+07, 1.03502e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.69173e+06, -1.04761e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55639e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.83459e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17294e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55639e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.53083e+12, 2.55652e+10 } } mol +Time: 3.10e+08 s, dt: 4320000 s, Cycle: 78 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.89e-03 ) ( Rwell ) = ( 1.98e-10 ) ( R ) = ( 2.89e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00260268 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569194 s | Solve Time: 0.331779 s + compositionalMultiphaseFlow: Max pressure change: 21429.647 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.821 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.722695710172701e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-03 ) ( Rwell ) = ( 3.18e-07 ) ( R ) = ( 1.82e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00234828 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.569933 s | Solve Time: 0.331327 s + compositionalMultiphaseFlow: Max pressure change: 11.845 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.719762112363583e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-06 ) ( Rwell ) = ( 1.35e-10 ) ( R ) = ( 1.44e-06 ) + Last LinSolve(iter,res) = ( 4, 2.35e-03 ) +wellControls1: BHP (at the specified reference elevation): 3605307.916031481 Pa +wellControls1: Total rate: -979.5821570280712 mol/s; total surface volumetric rate: -23.148148148453473 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148453473 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.282 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.594e+06, 1.00856e+07, 1.03334e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.71315e+06, -1.06344e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55216e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.82824e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16934e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55216e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.52664e+12, 2.55229e+10 } } mol +Time: 3.14e+08 s, dt: 1320000 s, Cycle: 79 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.85e-04 ) ( Rwell ) = ( 2.87e-10 ) ( R ) = ( 8.85e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00651621 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568237 s | Solve Time: 0.252331 s + compositionalMultiphaseFlow: Max pressure change: 6540.839 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.125 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.770171867565011e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.92e-04 ) ( Rwell ) = ( 3.00e-08 ) ( R ) = ( 4.92e-04 ) + Last LinSolve(iter,res) = ( 3, 6.52e-03 ) +wellControls1: BHP (at the specified reference elevation): 3594977.4379387344 Pa +wellControls1: Total rate: -979.5822085729202 mol/s; total surface volumetric rate: -23.14814814417943 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814417943 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.58746e+06, 1.00806e+07, 1.03283e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.73459e+06, -1.07927e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55087e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.8263e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16824e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55087e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.52536e+12, 2.55101e+10 } } mol +Time: 3.16e+08 s, dt: 2640000 s, Cycle: 80 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.83e-03 ) ( Rwell ) = ( 3.02e-08 ) ( R ) = ( 1.83e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00161078 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.568505 s | Solve Time: 0.330768 s + compositionalMultiphaseFlow: Max pressure change: 13128.409 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.152 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.821389510909711e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-04 ) ( Rwell ) = ( 1.23e-07 ) ( R ) = ( 4.53e-04 ) + Last LinSolve(iter,res) = ( 4, 1.61e-03 ) +wellControls1: BHP (at the specified reference elevation): 3574201.9373332392 Pa +wellControls1: Total rate: -979.5821575375679 mol/s; total surface volumetric rate: -23.148148155544177 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148155544177 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.173 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.57433e+06, 1.00706e+07, 1.0318e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.74113e+06, -1.08411e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54828e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.82242e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16604e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54828e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.5228e+12, 2.54842e+10 } } mol +Time: 3.18e+08 s, dt: 4320000 s, Cycle: 81 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.60e-03 ) ( Rwell ) = ( 1.24e-07 ) ( R ) = ( 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00261951 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.567934 s | Solve Time: 0.331558 s + compositionalMultiphaseFlow: Max pressure change: 21473.594 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.834 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.5102777007931536e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ( Rwell ) = ( 3.29e-07 ) ( R ) = ( 1.85e-03 ) + Last LinSolve(iter,res) = ( 4, 2.62e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00231959 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.56975 s | Solve Time: 0.331579 s + compositionalMultiphaseFlow: Max pressure change: 11.899 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.008641155272556e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-06 ) ( Rwell ) = ( 1.35e-10 ) ( R ) = ( 1.44e-06 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) +wellControls1: BHP (at the specified reference elevation): 3540129.9514768813 Pa +wellControls1: Total rate: -979.5821571874066 mol/s; total surface volumetric rate: -23.148148148238334 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148238334 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.284 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.55284e+06, 1.00542e+07, 1.03012e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.75426e+06, -1.09378e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54405e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.81608e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16244e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54405e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.51861e+12, 2.54419e+10 } } mol +Time: 3.23e+08 s, dt: 4320000 s, Cycle: 82 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.92e-03 ) ( Rwell ) = ( 2.91e-10 ) ( R ) = ( 2.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00260443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5817 s | Solve Time: 0.331735 s + compositionalMultiphaseFlow: Max pressure change: 21490.780 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.840 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.156839897439539e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-03 ) ( Rwell ) = ( 3.34e-07 ) ( R ) = ( 1.86e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00231246 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585297 s | Solve Time: 0.330298 s + compositionalMultiphaseFlow: Max pressure change: 12.147 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.1593249984534e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-06 ) ( Rwell ) = ( 1.34e-10 ) ( R ) = ( 1.44e-06 ) + Last LinSolve(iter,res) = ( 4, 2.31e-03 ) +wellControls1: BHP (at the specified reference elevation): 3505973.3079654374 Pa +wellControls1: Total rate: -979.5821583091022 mol/s; total surface volumetric rate: -23.148148148205728 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148205728 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.285 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.53134e+06, 1.00378e+07, 1.02844e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.77575e+06, -1.10961e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53982e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.80973e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.15885e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53982e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.51442e+12, 2.53996e+10 } } mol +Time: 3.27e+08 s, dt: 4320000 s, Cycle: 83 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-03 ) ( Rwell ) = ( 2.91e-10 ) ( R ) = ( 2.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00229269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581775 s | Solve Time: 0.330694 s + compositionalMultiphaseFlow: Max pressure change: 21512.820 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.846 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.316053062313756e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-03 ) ( Rwell ) = ( 3.40e-07 ) ( R ) = ( 1.81e-03 ) + Last LinSolve(iter,res) = ( 4, 2.29e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00194004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580672 s | Solve Time: 0.330162 s + compositionalMultiphaseFlow: Max pressure change: 11.720 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.092 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.316612603615937e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-06 ) ( Rwell ) = ( 6.45e-11 ) ( R ) = ( 1.04e-06 ) + Last LinSolve(iter,res) = ( 4, 1.94e-03 ) +wellControls1: BHP (at the specified reference elevation): 3471711.214177955 Pa +wellControls1: Total rate: -979.5821580691864 mol/s; total surface volumetric rate: -23.148148147988017 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147988017 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.286 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.50982e+06, 1.00214e+07, 1.02676e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.79725e+06, -1.12544e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53559e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.80338e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.15525e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53559e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.51023e+12, 2.53573e+10 } } mol +Time: 3.31e+08 s, dt: 4320000 s, Cycle: 84 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-03 ) ( Rwell ) = ( 2.23e-10 ) ( R ) = ( 2.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259731 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580417 s | Solve Time: 0.330745 s + compositionalMultiphaseFlow: Max pressure change: 21533.798 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.852 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.473109829905013e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ( Rwell ) = ( 3.46e-07 ) ( R ) = ( 1.89e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00228236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58339 s | Solve Time: 0.33056 s + compositionalMultiphaseFlow: Max pressure change: 12.377 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.099 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.471919681924845e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-06 ) ( Rwell ) = ( 1.30e-10 ) ( R ) = ( 1.43e-06 ) + Last LinSolve(iter,res) = ( 4, 2.28e-03 ) +wellControls1: BHP (at the specified reference elevation): 3437342.971704338 Pa +wellControls1: Total rate: -979.5821573865218 mol/s; total surface volumetric rate: -23.14814814822052 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814822052 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.287 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.48827e+06, 1.0005e+07, 1.02508e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.81877e+06, -1.14126e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53136e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.79703e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.15165e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53136e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.50604e+12, 2.5315e+10 } } mol +Time: 3.36e+08 s, dt: 4320000 s, Cycle: 85 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.95e-03 ) ( Rwell ) = ( 2.91e-10 ) ( R ) = ( 2.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259905 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579372 s | Solve Time: 0.330097 s + compositionalMultiphaseFlow: Max pressure change: 21555.404 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.859 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.627659580679904e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ( Rwell ) = ( 3.52e-07 ) ( R ) = ( 1.91e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00237898 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581636 s | Solve Time: 0.329999 s + compositionalMultiphaseFlow: Max pressure change: 12.511 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.098 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.627526698086086e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-06 ) ( Rwell ) = ( 1.35e-10 ) ( R ) = ( 1.48e-06 ) + Last LinSolve(iter,res) = ( 4, 2.38e-03 ) +wellControls1: BHP (at the specified reference elevation): 3402867.63459945 Pa +wellControls1: Total rate: -979.5821567161945 mol/s; total surface volumetric rate: -23.14814814801142 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814801142 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.288 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.4667e+06, 9.98867e+06, 1.0234e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.84032e+06, -1.15709e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52712e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.79069e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14806e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52712e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.50185e+12, 2.52728e+10 } } mol +Time: 3.40e+08 s, dt: 4320000 s, Cycle: 86 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.96e-03 ) ( Rwell ) = ( 2.98e-10 ) ( R ) = ( 2.96e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00246521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579243 s | Solve Time: 0.330144 s + compositionalMultiphaseFlow: Max pressure change: 21576.556 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.868 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.756514995906684e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ( Rwell ) = ( 3.59e-07 ) ( R ) = ( 1.90e-03 ) + Last LinSolve(iter,res) = ( 4, 2.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00215779 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578599 s | Solve Time: 0.330431 s + compositionalMultiphaseFlow: Max pressure change: 13.244 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.087 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.757277807942444e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-06 ) ( Rwell ) = ( 7.65e-11 ) ( R ) = ( 1.18e-06 ) + Last LinSolve(iter,res) = ( 4, 2.16e-03 ) +wellControls1: BHP (at the specified reference elevation): 3368284.141461271 Pa +wellControls1: Total rate: -979.5821562336035 mol/s; total surface volumetric rate: -23.14814814835615 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814835615 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.44511e+06, 9.9723e+06, 1.02172e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.86189e+06, -1.17292e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52289e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.78434e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14446e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52289e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.49766e+12, 2.52305e+10 } } mol +Time: 3.44e+08 s, dt: 3000000 s, Cycle: 87 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-03 ) ( Rwell ) = ( 2.42e-10 ) ( R ) = ( 2.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00173572 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583092 s | Solve Time: 0.330542 s + compositionalMultiphaseFlow: Max pressure change: 15002.220 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.774 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.787300089681423e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.20e-04 ) ( Rwell ) = ( 1.76e-07 ) ( R ) = ( 7.20e-04 ) + Last LinSolve(iter,res) = ( 4, 1.74e-03 ) +wellControls1: BHP (at the specified reference elevation): 3344224.727703623 Pa +wellControls1: Total rate: -979.5821393237989 mol/s; total surface volumetric rate: -23.14814815119872 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814815119872 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.202 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.43011e+06, 9.96093e+06, 1.02056e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.88348e+06, -1.18874e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51995e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.77993e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14196e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51995e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.49475e+12, 2.5201e+10 } } mol +Time: 3.47e+08 s, dt: 4320000 s, Cycle: 88 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-03 ) ( Rwell ) = ( 1.78e-07 ) ( R ) = ( 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00272593 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583397 s | Solve Time: 0.331283 s + compositionalMultiphaseFlow: Max pressure change: 21619.777 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.884 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.199697772351186e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-03 ) ( Rwell ) = ( 3.71e-07 ) ( R ) = ( 2.00e-03 ) + Last LinSolve(iter,res) = ( 4, 2.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00231552 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583661 s | Solve Time: 0.330346 s + compositionalMultiphaseFlow: Max pressure change: 12.498 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.092 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.986689608609822e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-06 ) ( Rwell ) = ( 9.63e-11 ) ( R ) = ( 1.33e-06 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) +wellControls1: BHP (at the specified reference elevation): 3309430.2584798154 Pa +wellControls1: Total rate: -979.5821439542401 mol/s; total surface volumetric rate: -23.148148148000445 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148000445 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.291 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.40848e+06, 9.94455e+06, 1.01888e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.89848e+06, -1.19973e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51572e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.77358e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13836e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51572e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.49056e+12, 2.51588e+10 } } mol +Time: 3.51e+08 s, dt: 4320000 s, Cycle: 89 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.00e-03 ) ( Rwell ) = ( 2.66e-10 ) ( R ) = ( 3.00e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00243968 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584357 s | Solve Time: 0.330022 s + compositionalMultiphaseFlow: Max pressure change: 21637.243 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.888 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.017350426124608e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-03 ) ( Rwell ) = ( 3.77e-07 ) ( R ) = ( 1.96e-03 ) + Last LinSolve(iter,res) = ( 4, 2.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00207588 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58294 s | Solve Time: 0.329773 s + compositionalMultiphaseFlow: Max pressure change: 11.692 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0174605014068305e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-06 ) ( Rwell ) = ( 6.41e-11 ) ( R ) = ( 1.19e-06 ) + Last LinSolve(iter,res) = ( 4, 2.08e-03 ) +wellControls1: BHP (at the specified reference elevation): 3274551.727563298 Pa +wellControls1: Total rate: -979.5821500422161 mol/s; total surface volumetric rate: -23.14814814791923 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814791923 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.292 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.38683e+06, 9.92818e+06, 1.0172e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.92011e+06, -1.21555e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51149e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.76724e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13477e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51149e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.48637e+12, 2.51165e+10 } } mol +Time: 3.56e+08 s, dt: 4320000 s, Cycle: 90 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-03 ) ( Rwell ) = ( 2.35e-10 ) ( R ) = ( 3.01e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00230015 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58294 s | Solve Time: 0.330214 s + compositionalMultiphaseFlow: Max pressure change: 21659.285 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.893 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0367521152687686e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-03 ) ( Rwell ) = ( 3.84e-07 ) ( R ) = ( 1.93e-03 ) + Last LinSolve(iter,res) = ( 4, 2.30e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00186479 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580806 s | Solve Time: 0.331578 s + compositionalMultiphaseFlow: Max pressure change: 12.483 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.091 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0366614511259087e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-06 ) ( Rwell ) = ( 6.26e-11 ) ( R ) = ( 1.06e-06 ) + Last LinSolve(iter,res) = ( 4, 1.86e-03 ) +wellControls1: BHP (at the specified reference elevation): 3239559.729202671 Pa +wellControls1: Total rate: -979.5821528289069 mol/s; total surface volumetric rate: -23.14814814763761 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814763761 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.293 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.36516e+06, 9.91181e+06, 1.01552e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.94176e+06, -1.23138e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50726e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.76089e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13117e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50726e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.48218e+12, 2.50742e+10 } } mol +Time: 3.60e+08 s, dt: 4320000 s, Cycle: 91 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.02e-03 ) ( Rwell ) = ( 2.36e-10 ) ( R ) = ( 3.02e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00260029 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581999 s | Solve Time: 0.331981 s + compositionalMultiphaseFlow: Max pressure change: 21681.383 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.898 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0539512895757497e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-03 ) ( Rwell ) = ( 3.91e-07 ) ( R ) = ( 2.01e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00220301 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585831 s | Solve Time: 0.331566 s + compositionalMultiphaseFlow: Max pressure change: 13.214 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.098 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0538244121782725e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-06 ) ( Rwell ) = ( 1.26e-10 ) ( R ) = ( 1.42e-06 ) + Last LinSolve(iter,res) = ( 4, 2.20e-03 ) +wellControls1: BHP (at the specified reference elevation): 3204453.616085096 Pa +wellControls1: Total rate: -979.5821539944793 mol/s; total surface volumetric rate: -23.148148148053963 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148053963 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.295 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.34346e+06, 9.89543e+06, 1.01384e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.96343e+06, -1.2472e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50303e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.75454e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12757e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50303e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.47799e+12, 2.50319e+10 } } mol +Time: 3.64e+08 s, dt: 4320000 s, Cycle: 92 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-03 ) ( Rwell ) = ( 3.03e-10 ) ( R ) = ( 3.03e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00260207 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582075 s | Solve Time: 0.331273 s + compositionalMultiphaseFlow: Max pressure change: 21704.164 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.905 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0714066667194544e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-03 ) ( Rwell ) = ( 3.99e-07 ) ( R ) = ( 2.03e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00220504 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579317 s | Solve Time: 0.331117 s + compositionalMultiphaseFlow: Max pressure change: 13.336 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.098 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0714039799797348e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-06 ) ( Rwell ) = ( 1.25e-10 ) ( R ) = ( 1.38e-06 ) + Last LinSolve(iter,res) = ( 4, 2.21e-03 ) +wellControls1: BHP (at the specified reference elevation): 3169232.4810188687 Pa +wellControls1: Total rate: -979.5821544697002 mol/s; total surface volumetric rate: -23.148148148046587 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148046587 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.32175e+06, 9.87906e+06, 1.01216e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -3.98513e+06, -1.26302e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49879e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.74819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12398e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49879e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.47381e+12, 2.49897e+10 } } mol +Time: 3.69e+08 s, dt: 4320000 s, Cycle: 93 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-03 ) ( Rwell ) = ( 3.04e-10 ) ( R ) = ( 3.04e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00247707 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581216 s | Solve Time: 0.331251 s + compositionalMultiphaseFlow: Max pressure change: 21726.453 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.914 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0860289978431581e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-03 ) ( Rwell ) = ( 4.06e-07 ) ( R ) = ( 2.02e-03 ) + Last LinSolve(iter,res) = ( 4, 2.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0021635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579812 s | Solve Time: 0.331877 s + compositionalMultiphaseFlow: Max pressure change: 14.078 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.086 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0861692623098662e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-06 ) ( Rwell ) = ( 7.83e-11 ) ( R ) = ( 1.22e-06 ) + Last LinSolve(iter,res) = ( 4, 2.16e-03 ) +wellControls1: BHP (at the specified reference elevation): 3133895.2392417733 Pa +wellControls1: Total rate: -979.5821546857084 mol/s; total surface volumetric rate: -23.148148147994018 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147994018 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.297 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.30001e+06, 9.86269e+06, 1.01048e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.00684e+06, -1.27884e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49456e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.74184e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12038e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49456e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.46962e+12, 2.49474e+10 } } mol +Time: 3.73e+08 s, dt: 4320000 s, Cycle: 94 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-03 ) ( Rwell ) = ( 2.59e-10 ) ( R ) = ( 3.06e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00266954 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579027 s | Solve Time: 0.331996 s + compositionalMultiphaseFlow: Max pressure change: 21750.881 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.920 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1052536230682364e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-03 ) ( Rwell ) = ( 4.14e-07 ) ( R ) = ( 2.08e-03 ) + Last LinSolve(iter,res) = ( 4, 2.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0023158 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577675 s | Solve Time: 0.331767 s + compositionalMultiphaseFlow: Max pressure change: 12.820 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.092 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1054085868877905e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-06 ) ( Rwell ) = ( 8.97e-11 ) ( R ) = ( 1.32e-06 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) +wellControls1: BHP (at the specified reference elevation): 3098440.74544176 Pa +wellControls1: Total rate: -979.582154842236 mol/s; total surface volumetric rate: -23.1481481482183 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.1481481482183 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.298 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.27824e+06, 9.84632e+06, 1.0088e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.02859e+06, -1.29466e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49033e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.7355e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11678e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49033e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.46543e+12, 2.49051e+10 } } mol +Time: 3.77e+08 s, dt: 1320000 s, Cycle: 95 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-04 ) ( Rwell ) = ( 2.74e-10 ) ( R ) = ( 9.38e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00642937 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582452 s | Solve Time: 0.25244 s + compositionalMultiphaseFlow: Max pressure change: 6639.119 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.153 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.990365008010315e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-04 ) ( Rwell ) = ( 3.92e-08 ) ( R ) = ( 5.01e-04 ) + Last LinSolve(iter,res) = ( 3, 6.43e-03 ) +wellControls1: BHP (at the specified reference elevation): 3087620.8938695807 Pa +wellControls1: Total rate: -979.5822063855466 mol/s; total surface volumetric rate: -23.14814814348949 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814348949 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.2716e+06, 9.84131e+06, 1.00829e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.05035e+06, -1.31048e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48904e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.73356e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11568e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48904e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.46415e+12, 2.48922e+10 } } mol +Time: 3.79e+08 s, dt: 2640000 s, Cycle: 96 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ( Rwell ) = ( 3.95e-08 ) ( R ) = ( 1.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00155271 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580034 s | Solve Time: 0.331259 s + compositionalMultiphaseFlow: Max pressure change: 13327.533 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.211 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.512642110514719e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-04 ) ( Rwell ) = ( 1.62e-07 ) ( R ) = ( 5.11e-04 ) + Last LinSolve(iter,res) = ( 4, 1.55e-03 ) +wellControls1: BHP (at the specified reference elevation): 3065857.710398565 Pa +wellControls1: Total rate: -979.5821515721557 mol/s; total surface volumetric rate: -23.148148157195724 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148157195724 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.183 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.25827e+06, 9.83131e+06, 1.00726e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.05699e+06, -1.31531e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48645e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.72968e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11348e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48645e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.46159e+12, 2.48664e+10 } } mol +Time: 3.81e+08 s, dt: 4320000 s, Cycle: 97 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-03 ) ( Rwell ) = ( 1.64e-07 ) ( R ) = ( 2.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00231557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582329 s | Solve Time: 0.33157 s + compositionalMultiphaseFlow: Max pressure change: 21799.369 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.933 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.977099109573004e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-03 ) ( Rwell ) = ( 4.31e-07 ) ( R ) = ( 2.04e-03 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00178148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579848 s | Solve Time: 0.331699 s + compositionalMultiphaseFlow: Max pressure change: 13.049 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.092 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1387887599578761e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-06 ) ( Rwell ) = ( 5.55e-11 ) ( R ) = ( 1.06e-06 ) + Last LinSolve(iter,res) = ( 4, 1.78e-03 ) +wellControls1: BHP (at the specified reference elevation): 3030153.7908468293 Pa +wellControls1: Total rate: -979.5821529453934 mol/s; total surface volumetric rate: -23.148148148083912 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148083912 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.301 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.23646e+06, 9.81494e+06, 1.00558e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.07032e+06, -1.32498e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48222e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.72333e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10989e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48222e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.4574e+12, 2.48241e+10 } } mol +Time: 3.86e+08 s, dt: 4320000 s, Cycle: 98 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.09e-03 ) ( Rwell ) = ( 2.44e-10 ) ( R ) = ( 3.09e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00247844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577283 s | Solve Time: 0.331204 s + compositionalMultiphaseFlow: Max pressure change: 21817.937 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.942 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1536917288168524e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-03 ) ( Rwell ) = ( 4.39e-07 ) ( R ) = ( 2.10e-03 ) + Last LinSolve(iter,res) = ( 4, 2.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00204919 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583069 s | Solve Time: 0.331646 s + compositionalMultiphaseFlow: Max pressure change: 14.182 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.088 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1535137101059689e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-06 ) ( Rwell ) = ( 7.55e-11 ) ( R ) = ( 1.21e-06 ) + Last LinSolve(iter,res) = ( 4, 2.05e-03 ) +wellControls1: BHP (at the specified reference elevation): 2994350.5986597626 Pa +wellControls1: Total rate: -979.5821546982471 mol/s; total surface volumetric rate: -23.148148148194483 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148194483 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.302 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.21463e+06, 9.79856e+06, 1.0039e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.09213e+06, -1.3408e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47799e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.71698e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10629e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47799e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.45321e+12, 2.47818e+10 } } mol +Time: 3.90e+08 s, dt: 4320000 s, Cycle: 99 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.11e-03 ) ( Rwell ) = ( 2.67e-10 ) ( R ) = ( 3.11e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00260065 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581518 s | Solve Time: 0.331446 s + compositionalMultiphaseFlow: Max pressure change: 21842.193 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.947 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1750283623879199e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-03 ) ( Rwell ) = ( 4.48e-07 ) ( R ) = ( 2.14e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00213675 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5831 s | Solve Time: 0.331896 s + compositionalMultiphaseFlow: Max pressure change: 13.976 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1749642025993268e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-06 ) ( Rwell ) = ( 1.29e-10 ) ( R ) = ( 1.40e-06 ) + Last LinSolve(iter,res) = ( 4, 2.14e-03 ) +wellControls1: BHP (at the specified reference elevation): 2958424.5658170674 Pa +wellControls1: Total rate: -979.5821547304652 mol/s; total surface volumetric rate: -23.148148148020915 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148020915 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.303 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.19277e+06, 9.78219e+06, 1.00222e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.11396e+06, -1.35662e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47376e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.71063e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10269e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47376e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.44902e+12, 2.47395e+10 } } mol +Time: 3.94e+08 s, dt: 4320000 s, Cycle: 100 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.12e-03 ) ( Rwell ) = ( 3.24e-10 ) ( R ) = ( 3.12e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0024548 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.576929 s | Solve Time: 0.332078 s + compositionalMultiphaseFlow: Max pressure change: 21867.225 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.953 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1942348010496318e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-03 ) ( Rwell ) = ( 4.57e-07 ) ( R ) = ( 2.15e-03 ) + Last LinSolve(iter,res) = ( 4, 2.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00198894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577649 s | Solve Time: 0.331617 s + compositionalMultiphaseFlow: Max pressure change: 13.036 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1945144362535132e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-06 ) ( Rwell ) = ( 5.81e-11 ) ( R ) = ( 1.23e-06 ) + Last LinSolve(iter,res) = ( 4, 1.99e-03 ) +wellControls1: BHP (at the specified reference elevation): 2922374.7572888504 Pa +wellControls1: Total rate: -979.5821542921075 mol/s; total surface volumetric rate: -23.148148148490385 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148490385 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.304 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.17089e+06, 9.76582e+06, 1.00054e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.13582e+06, -1.37244e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46952e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.70429e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0991e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46952e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.44483e+12, 2.46972e+10 } } mol +Time: 3.99e+08 s, dt: 4320000 s, Cycle: 101 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.13e-03 ) ( Rwell ) = ( 2.56e-10 ) ( R ) = ( 3.13e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259239 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580572 s | Solve Time: 0.332301 s + compositionalMultiphaseFlow: Max pressure change: 21890.277 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.961 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2116096681502597e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-03 ) ( Rwell ) = ( 4.67e-07 ) ( R ) = ( 2.17e-03 ) + Last LinSolve(iter,res) = ( 4, 2.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00209804 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581505 s | Solve Time: 0.331698 s + compositionalMultiphaseFlow: Max pressure change: 14.214 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.211336291273568e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-06 ) ( Rwell ) = ( 1.25e-10 ) ( R ) = ( 1.43e-06 ) + Last LinSolve(iter,res) = ( 4, 2.10e-03 ) +wellControls1: BHP (at the specified reference elevation): 2886199.9811720923 Pa +wellControls1: Total rate: -979.5821537405859 mol/s; total surface volumetric rate: -23.14814814845283 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814845283 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.14899e+06, 9.74945e+06, 9.98862e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.1577e+06, -1.38825e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46529e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.69794e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0955e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46529e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.44064e+12, 2.4655e+10 } } mol +Time: 4.03e+08 s, dt: 4320000 s, Cycle: 102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.15e-03 ) ( Rwell ) = ( 3.27e-10 ) ( R ) = ( 3.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0024579 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5789 s | Solve Time: 0.332 s + compositionalMultiphaseFlow: Max pressure change: 21915.571 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.967 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2313664965457605e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-03 ) ( Rwell ) = ( 4.77e-07 ) ( R ) = ( 2.19e-03 ) + Last LinSolve(iter,res) = ( 4, 2.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00199387 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581574 s | Solve Time: 0.33224 s + compositionalMultiphaseFlow: Max pressure change: 13.306 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2316946296220266e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-06 ) ( Rwell ) = ( 5.89e-11 ) ( R ) = ( 1.27e-06 ) + Last LinSolve(iter,res) = ( 4, 1.99e-03 ) +wellControls1: BHP (at the specified reference elevation): 2849898.922501278 Pa +wellControls1: Total rate: -979.5821533446162 mol/s; total surface volumetric rate: -23.148148148284772 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148284772 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.307 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.12706e+06, 9.73308e+06, 9.97183e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.1796e+06, -1.40407e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46106e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.69159e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0919e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46106e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.43645e+12, 2.46127e+10 } } mol +Time: 4.07e+08 s, dt: 3000000 s, Cycle: 103 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-03 ) ( Rwell ) = ( 2.63e-10 ) ( R ) = ( 2.19e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00173711 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584765 s | Solve Time: 0.332435 s + compositionalMultiphaseFlow: Max pressure change: 15238.594 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.843 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.031828592156785e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.03e-04 ) ( Rwell ) = ( 2.35e-07 ) ( R ) = ( 8.03e-04 ) + Last LinSolve(iter,res) = ( 4, 1.74e-03 ) +wellControls1: BHP (at the specified reference elevation): 2824639.933657005 Pa +wellControls1: Total rate: -979.5821336576814 mol/s; total surface volumetric rate: -23.148148152472984 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148152472984 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.11182e+06, 9.72171e+06, 9.96016e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.20153e+06, -1.41988e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.45812e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.68718e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0894e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.45812e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.43354e+12, 2.45832e+10 } } mol +Time: 4.10e+08 s, dt: 4320000 s, Cycle: 104 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.63e-03 ) ( Rwell ) = ( 2.37e-07 ) ( R ) = ( 2.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0025016 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583286 s | Solve Time: 0.33187 s + compositionalMultiphaseFlow: Max pressure change: 21961.136 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.988 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.503860938700257e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-03 ) ( Rwell ) = ( 4.95e-07 ) ( R ) = ( 2.22e-03 ) + Last LinSolve(iter,res) = ( 4, 2.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00197948 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577703 s | Solve Time: 0.332032 s + compositionalMultiphaseFlow: Max pressure change: 15.130 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.087 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.253421612057437e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-06 ) ( Rwell ) = ( 7.21e-11 ) ( R ) = ( 1.23e-06 ) + Last LinSolve(iter,res) = ( 4, 1.98e-03 ) +wellControls1: BHP (at the specified reference elevation): 2788092.3126613656 Pa +wellControls1: Total rate: -979.5821398626786 mol/s; total surface volumetric rate: -23.148148148056475 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148056475 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.309 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.08985e+06, 9.70534e+06, 9.94337e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.21677e+06, -1.43087e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.45389e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.68084e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08581e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.45389e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.42935e+12, 2.4541e+10 } } mol +Time: 4.15e+08 s, dt: 4320000 s, Cycle: 105 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-03 ) ( Rwell ) = ( 2.82e-10 ) ( R ) = ( 3.18e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00273934 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5781 s | Solve Time: 0.331044 s + compositionalMultiphaseFlow: Max pressure change: 21979.259 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.995 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.271932797974884e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-03 ) ( Rwell ) = ( 5.05e-07 ) ( R ) = ( 2.31e-03 ) + Last LinSolve(iter,res) = ( 4, 2.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00227669 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580101 s | Solve Time: 0.331758 s + compositionalMultiphaseFlow: Max pressure change: 15.672 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.088 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2717861141986475e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-06 ) ( Rwell ) = ( 9.36e-11 ) ( R ) = ( 1.43e-06 ) + Last LinSolve(iter,res) = ( 4, 2.28e-03 ) +wellControls1: BHP (at the specified reference elevation): 2751445.98250896 Pa +wellControls1: Total rate: -979.5821463771539 mol/s; total surface volumetric rate: -23.148148147931252 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148147931252 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.310 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.06785e+06, 9.68897e+06, 9.92658e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.23874e+06, -1.44668e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44966e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.67449e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08221e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44966e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.42516e+12, 2.44987e+10 } } mol +Time: 4.19e+08 s, dt: 4320000 s, Cycle: 106 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-03 ) ( Rwell ) = ( 3.07e-10 ) ( R ) = ( 3.19e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00224662 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579602 s | Solve Time: 0.331619 s + compositionalMultiphaseFlow: Max pressure change: 22005.551 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 6.997 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.299073912885973e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-03 ) ( Rwell ) = ( 5.16e-07 ) ( R ) = ( 2.22e-03 ) + Last LinSolve(iter,res) = ( 4, 2.25e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00163607 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581599 s | Solve Time: 0.331536 s + compositionalMultiphaseFlow: Max pressure change: 14.792 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.090 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.299391363396296e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-06 ) ( Rwell ) = ( 3.23e-11 ) ( R ) = ( 1.06e-06 ) + Last LinSolve(iter,res) = ( 4, 1.64e-03 ) +wellControls1: BHP (at the specified reference elevation): 2714667.028478903 Pa +wellControls1: Total rate: -979.58214948715 mol/s; total surface volumetric rate: -23.148148148356686 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148356686 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.312 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.04583e+06, 9.6726e+06, 9.90978e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.26074e+06, -1.46249e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44543e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.66814e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07861e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44543e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.42097e+12, 2.44564e+10 } } mol +Time: 4.23e+08 s, dt: 4320000 s, Cycle: 107 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.21e-03 ) ( Rwell ) = ( 2.49e-10 ) ( R ) = ( 3.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00260067 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580064 s | Solve Time: 0.331474 s + compositionalMultiphaseFlow: Max pressure change: 22030.759 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.004 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3186747471749527e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-03 ) ( Rwell ) = ( 5.28e-07 ) ( R ) = ( 2.30e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00203666 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585874 s | Solve Time: 0.331673 s + compositionalMultiphaseFlow: Max pressure change: 15.022 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.318427114149756e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-06 ) ( Rwell ) = ( 1.24e-10 ) ( R ) = ( 1.40e-06 ) + Last LinSolve(iter,res) = ( 4, 2.04e-03 ) +wellControls1: BHP (at the specified reference elevation): 2677754.5218267944 Pa +wellControls1: Total rate: -979.5821507771835 mol/s; total surface volumetric rate: -23.14814814787981 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814787981 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.02378e+06, 9.65623e+06, 9.89299e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.28276e+06, -1.47831e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.4412e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.66179e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07502e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.4412e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.41678e+12, 2.44142e+10 } } mol +Time: 4.28e+08 s, dt: 4320000 s, Cycle: 108 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-03 ) ( Rwell ) = ( 3.46e-10 ) ( R ) = ( 3.22e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00249662 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584382 s | Solve Time: 0.331286 s + compositionalMultiphaseFlow: Max pressure change: 22055.529 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.012 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.337627377751005e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-03 ) ( Rwell ) = ( 5.40e-07 ) ( R ) = ( 2.31e-03 ) + Last LinSolve(iter,res) = ( 4, 2.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00194081 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580843 s | Solve Time: 0.331446 s + compositionalMultiphaseFlow: Max pressure change: 15.801 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.087 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3376723528857326e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-06 ) ( Rwell ) = ( 6.99e-11 ) ( R ) = ( 1.24e-06 ) + Last LinSolve(iter,res) = ( 4, 1.94e-03 ) +wellControls1: BHP (at the specified reference elevation): 2640707.239953071 Pa +wellControls1: Total rate: -979.5821514208266 mol/s; total surface volumetric rate: -23.148148148417754 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148417754 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.314 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 7.00171e+06, 9.63986e+06, 9.87619e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.30481e+06, -1.49412e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43696e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.65545e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07142e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43696e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.41259e+12, 2.43719e+10 } } mol +Time: 4.32e+08 s, dt: 4320000 s, Cycle: 109 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-03 ) ( Rwell ) = ( 2.95e-10 ) ( R ) = ( 3.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259451 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.57793 s | Solve Time: 0.331491 s + compositionalMultiphaseFlow: Max pressure change: 22081.756 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.019 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3593290248969936e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-03 ) ( Rwell ) = ( 5.52e-07 ) ( R ) = ( 2.35e-03 ) + Last LinSolve(iter,res) = ( 4, 2.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00200245 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580201 s | Solve Time: 0.331083 s + compositionalMultiphaseFlow: Max pressure change: 15.272 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.359165654468697e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-06 ) ( Rwell ) = ( 1.20e-10 ) ( R ) = ( 1.40e-06 ) + Last LinSolve(iter,res) = ( 4, 2.00e-03 ) +wellControls1: BHP (at the specified reference elevation): 2603523.821707543 Pa +wellControls1: Total rate: -979.5821517328469 mol/s; total surface volumetric rate: -23.148148148062294 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148062294 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.316 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.97962e+06, 9.62349e+06, 9.8594e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.32688e+06, -1.50993e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43273e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.6491e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06782e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43273e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.4084e+12, 2.43296e+10 } } mol +Time: 4.36e+08 s, dt: 4320000 s, Cycle: 110 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-03 ) ( Rwell ) = ( 3.50e-10 ) ( R ) = ( 3.25e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0025581 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579689 s | Solve Time: 0.331434 s + compositionalMultiphaseFlow: Max pressure change: 22107.209 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.027 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3791937392149123e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-03 ) ( Rwell ) = ( 5.65e-07 ) ( R ) = ( 2.35e-03 ) + Last LinSolve(iter,res) = ( 4, 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00197164 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581987 s | Solve Time: 0.331888 s + compositionalMultiphaseFlow: Max pressure change: 15.695 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.091 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.379533263179411e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-06 ) ( Rwell ) = ( 6.84e-11 ) ( R ) = ( 1.22e-06 ) + Last LinSolve(iter,res) = ( 4, 1.97e-03 ) +wellControls1: BHP (at the specified reference elevation): 2566202.7704051766 Pa +wellControls1: Total rate: -979.5821520144715 mol/s; total surface volumetric rate: -23.148148148241443 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148241443 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.95749e+06, 9.60711e+06, 9.84261e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.34897e+06, -1.52574e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.4285e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.64275e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06422e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.4285e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.40421e+12, 2.42873e+10 } } mol +Time: 4.41e+08 s, dt: 1320000 s, Cycle: 111 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.97e-04 ) ( Rwell ) = ( 3.01e-10 ) ( R ) = ( 9.97e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00649126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578398 s | Solve Time: 0.252648 s + compositionalMultiphaseFlow: Max pressure change: 6748.602 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.184 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1472576777471488e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.08e-04 ) ( Rwell ) = ( 5.37e-08 ) ( R ) = ( 5.08e-04 ) + Last LinSolve(iter,res) = ( 3, 6.49e-03 ) +wellControls1: BHP (at the specified reference elevation): 2554811.173853319 Pa +wellControls1: Total rate: -979.5822038853124 mol/s; total surface volumetric rate: -23.148148142393243 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148142393243 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.097 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.95074e+06, 9.60211e+06, 9.83747e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.3711e+06, -1.54155e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42721e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.64081e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06313e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42721e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.40293e+12, 2.42745e+10 } } mol +Time: 4.42e+08 s, dt: 2640000 s, Cycle: 112 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-03 ) ( Rwell ) = ( 5.41e-08 ) ( R ) = ( 2.05e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00991109 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.577031 s | Solve Time: 0.252347 s + compositionalMultiphaseFlow: Max pressure change: 13510.143 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.356 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.610706167389566e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 2.17e-07 ) ( R ) = ( 1.26e-03 ) + Last LinSolve(iter,res) = ( 3, 9.91e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00937057 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580269 s | Solve Time: 0.252819 s + compositionalMultiphaseFlow: Max pressure change: 41.139 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.164 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.6731019054391254e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-05 ) ( Rwell ) = ( 3.88e-09 ) ( R ) = ( 1.28e-05 ) + Last LinSolve(iter,res) = ( 3, 9.37e-03 ) +wellControls1: BHP (at the specified reference elevation): 2531875.8943874165 Pa +wellControls1: Total rate: -979.5821660121891 mol/s; total surface volumetric rate: -23.148148148124953 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148124953 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.93719e+06, 9.59211e+06, 9.82721e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.37785e+06, -1.54638e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42462e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.63693e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06093e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42462e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.40037e+12, 2.42486e+10 } } mol +Time: 4.44e+08 s, dt: 4320000 s, Cycle: 113 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-03 ) ( Rwell ) = ( 4.15e-09 ) ( R ) = ( 3.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00226239 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578655 s | Solve Time: 0.332021 s + compositionalMultiphaseFlow: Max pressure change: 22158.687 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.036 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4189108621387447e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-03 ) ( Rwell ) = ( 5.92e-07 ) ( R ) = ( 2.36e-03 ) + Last LinSolve(iter,res) = ( 4, 2.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00157967 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580858 s | Solve Time: 0.33212 s + compositionalMultiphaseFlow: Max pressure change: 15.572 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.089 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.427389496599929e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-06 ) ( Rwell ) = ( 2.81e-11 ) ( R ) = ( 1.10e-06 ) + Last LinSolve(iter,res) = ( 4, 1.58e-03 ) +wellControls1: BHP (at the specified reference elevation): 2494283.2888208227 Pa +wellControls1: Total rate: -979.582159217638 mol/s; total surface volumetric rate: -23.148148148157663 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148157663 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.320 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.91502e+06, 9.57574e+06, 9.81042e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.3914e+06, -1.55604e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42039e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.63058e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05733e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42039e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.39618e+12, 2.42063e+10 } } mol +Time: 4.49e+08 s, dt: 4320000 s, Cycle: 114 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.29e-03 ) ( Rwell ) = ( 2.69e-10 ) ( R ) = ( 3.29e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00249432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580454 s | Solve Time: 0.331616 s + compositionalMultiphaseFlow: Max pressure change: 22183.403 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.048 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4426939654033077e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-03 ) ( Rwell ) = ( 6.05e-07 ) ( R ) = ( 2.43e-03 ) + Last LinSolve(iter,res) = ( 4, 2.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00186842 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579528 s | Solve Time: 0.33182 s + compositionalMultiphaseFlow: Max pressure change: 16.488 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.087 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4427283190343587e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-06 ) ( Rwell ) = ( 6.57e-11 ) ( R ) = ( 1.26e-06 ) + Last LinSolve(iter,res) = ( 4, 1.87e-03 ) +wellControls1: BHP (at the specified reference elevation): 2456550.610641578 Pa +wellControls1: Total rate: -979.5821555761984 mol/s; total surface volumetric rate: -23.148148148152874 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148152874 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.89282e+06, 9.55937e+06, 9.79362e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.41357e+06, -1.57185e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41616e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.62424e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05373e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41616e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.39199e+12, 2.4164e+10 } } mol +Time: 4.53e+08 s, dt: 4320000 s, Cycle: 115 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-03 ) ( Rwell ) = ( 3.12e-10 ) ( R ) = ( 3.31e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579232 s | Solve Time: 0.331307 s + compositionalMultiphaseFlow: Max pressure change: 22210.345 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.055 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4638858147897338e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e-03 ) ( Rwell ) = ( 6.20e-07 ) ( R ) = ( 2.47e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00196788 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580434 s | Solve Time: 0.327855 s + compositionalMultiphaseFlow: Max pressure change: 16.075 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.463605086016173e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-06 ) ( Rwell ) = ( 1.15e-10 ) ( R ) = ( 1.47e-06 ) + Last LinSolve(iter,res) = ( 4, 1.97e-03 ) +wellControls1: BHP (at the specified reference elevation): 2418674.4908646033 Pa +wellControls1: Total rate: -979.5821534858087 mol/s; total surface volumetric rate: -23.14814814824099 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814824099 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.87059e+06, 9.543e+06, 9.77683e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.43577e+06, -1.58766e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41193e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.61789e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05014e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41193e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.3878e+12, 2.41218e+10 } } mol +Time: 4.57e+08 s, dt: 4320000 s, Cycle: 116 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.32e-03 ) ( Rwell ) = ( 3.66e-10 ) ( R ) = ( 3.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00275426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578797 s | Solve Time: 0.332537 s + compositionalMultiphaseFlow: Max pressure change: 22236.041 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.066 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4812208892767131e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-03 ) ( Rwell ) = ( 6.35e-07 ) ( R ) = ( 2.54e-03 ) + Last LinSolve(iter,res) = ( 4, 2.75e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00207376 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579843 s | Solve Time: 0.332421 s + compositionalMultiphaseFlow: Max pressure change: 17.160 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.088 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4813262583235343e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-06 ) ( Rwell ) = ( 9.07e-11 ) ( R ) = ( 1.45e-06 ) + Last LinSolve(iter,res) = ( 4, 2.07e-03 ) +wellControls1: BHP (at the specified reference elevation): 2380653.0804172014 Pa +wellControls1: Total rate: -979.5821523078683 mol/s; total surface volumetric rate: -23.14814814816796 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814816796 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.84834e+06, 9.52663e+06, 9.76004e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.458e+06, -1.60347e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40769e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.61154e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04654e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40769e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.38361e+12, 2.40795e+10 } } mol +Time: 4.62e+08 s, dt: 4320000 s, Cycle: 117 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-03 ) ( Rwell ) = ( 3.47e-10 ) ( R ) = ( 3.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00259678 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579194 s | Solve Time: 0.332269 s + compositionalMultiphaseFlow: Max pressure change: 22263.414 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.073 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5051011714728446e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-03 ) ( Rwell ) = ( 6.51e-07 ) ( R ) = ( 2.54e-03 ) + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00189883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.578126 s | Solve Time: 0.332221 s + compositionalMultiphaseFlow: Max pressure change: 16.820 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.094 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.505235546206407e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-06 ) ( Rwell ) = ( 1.04e-10 ) ( R ) = ( 1.41e-06 ) + Last LinSolve(iter,res) = ( 4, 1.90e-03 ) +wellControls1: BHP (at the specified reference elevation): 2342484.571432929 Pa +wellControls1: Total rate: -979.5821517333648 mol/s; total surface volumetric rate: -23.14814814823795 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814823795 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.325 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.82606e+06, 9.51026e+06, 9.74324e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.48025e+06, -1.61928e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40346e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.60519e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04294e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40346e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.37942e+12, 2.40372e+10 } } mol +Time: 4.66e+08 s, dt: 4320000 s, Cycle: 118 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-03 ) ( Rwell ) = ( 3.65e-10 ) ( R ) = ( 3.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00249376 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582814 s | Solve Time: 0.330944 s + compositionalMultiphaseFlow: Max pressure change: 22290.383 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.082 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5263568076129275e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-03 ) ( Rwell ) = ( 6.68e-07 ) ( R ) = ( 2.53e-03 ) + Last LinSolve(iter,res) = ( 4, 2.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00181181 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581265 s | Solve Time: 0.331477 s + compositionalMultiphaseFlow: Max pressure change: 17.103 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.086 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.526175584798395e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-06 ) ( Rwell ) = ( 5.93e-11 ) ( R ) = ( 1.28e-06 ) + Last LinSolve(iter,res) = ( 4, 1.81e-03 ) +wellControls1: BHP (at the specified reference elevation): 2304167.1820672094 Pa +wellControls1: Total rate: -979.5821515237932 mol/s; total surface volumetric rate: -23.148148148386127 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148386127 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.327 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.80375e+06, 9.49389e+06, 9.72645e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.50253e+06, -1.63508e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39923e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.59885e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03935e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39923e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.37524e+12, 2.39949e+10 } } mol +Time: 4.70e+08 s, dt: 3000000 s, Cycle: 119 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.34e-03 ) ( Rwell ) = ( 3.25e-10 ) ( R ) = ( 2.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00167554 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583514 s | Solve Time: 0.331899 s + compositionalMultiphaseFlow: Max pressure change: 15502.692 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.921 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.49183425297062e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.51e-04 ) ( Rwell ) = ( 3.31e-07 ) ( R ) = ( 9.51e-04 ) + Last LinSolve(iter,res) = ( 4, 1.68e-03 ) +wellControls1: BHP (at the specified reference elevation): 2277499.7082193308 Pa +wellControls1: Total rate: -979.5821317469802 mol/s; total surface volumetric rate: -23.148148153763145 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148153763145 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.228 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.78825e+06, 9.48252e+06, 9.71479e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.52484e+06, -1.65089e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39629e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.59444e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03685e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39629e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.37233e+12, 2.39655e+10 } } mol +Time: 4.73e+08 s, dt: 4320000 s, Cycle: 120 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-03 ) ( Rwell ) = ( 3.35e-07 ) ( R ) = ( 2.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00250514 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580928 s | Solve Time: 0.33196 s + compositionalMultiphaseFlow: Max pressure change: 22343.274 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.102 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.080796343179486e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.59e-03 ) ( Rwell ) = ( 6.99e-07 ) ( R ) = ( 2.59e-03 ) + Last LinSolve(iter,res) = ( 4, 2.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00178795 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584023 s | Solve Time: 0.331404 s + compositionalMultiphaseFlow: Max pressure change: 17.261 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.087 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5573471723318022e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-06 ) ( Rwell ) = ( 5.92e-11 ) ( R ) = ( 1.29e-06 ) + Last LinSolve(iter,res) = ( 4, 1.79e-03 ) +wellControls1: BHP (at the specified reference elevation): 2238890.8399785217 Pa +wellControls1: Total rate: -979.5821376185489 mol/s; total surface volumetric rate: -23.148148148071208 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148071208 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.76589e+06, 9.46615e+06, 9.698e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.54034e+06, -1.66187e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39206e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.58809e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03325e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39206e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.36814e+12, 2.39232e+10 } } mol +Time: 4.78e+08 s, dt: 4320000 s, Cycle: 121 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-03 ) ( Rwell ) = ( 3.35e-10 ) ( R ) = ( 3.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00231782 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586894 s | Solve Time: 0.331706 s + compositionalMultiphaseFlow: Max pressure change: 22365.124 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.107 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5837124256457003e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-03 ) ( Rwell ) = ( 7.16e-07 ) ( R ) = ( 2.57e-03 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00157604 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586008 s | Solve Time: 0.331785 s + compositionalMultiphaseFlow: Max pressure change: 16.300 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.090 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.583691991990932e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-06 ) ( Rwell ) = ( 3.91e-11 ) ( R ) = ( 1.20e-06 ) + Last LinSolve(iter,res) = ( 4, 1.58e-03 ) +wellControls1: BHP (at the specified reference elevation): 2200165.377062335 Pa +wellControls1: Total rate: -979.58214468785 mol/s; total surface volumetric rate: -23.148148148400033 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148400033 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.331 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.74351e+06, 9.44978e+06, 9.6812e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.5627e+06, -1.67767e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.38783e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.58174e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02965e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.38783e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.36395e+12, 2.38809e+10 } } mol +Time: 4.82e+08 s, dt: 4320000 s, Cycle: 122 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.41e-03 ) ( Rwell ) = ( 3.20e-10 ) ( R ) = ( 3.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00248803 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582815 s | Solve Time: 0.331376 s + compositionalMultiphaseFlow: Max pressure change: 22392.236 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.115 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.606214430349695e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-03 ) ( Rwell ) = ( 7.36e-07 ) ( R ) = ( 2.64e-03 ) + Last LinSolve(iter,res) = ( 4, 2.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00182998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580695 s | Solve Time: 0.333978 s + compositionalMultiphaseFlow: Max pressure change: 17.624 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.086 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6062389318616255e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-06 ) ( Rwell ) = ( 6.12e-11 ) ( R ) = ( 1.32e-06 ) + Last LinSolve(iter,res) = ( 4, 1.83e-03 ) +wellControls1: BHP (at the specified reference elevation): 2161283.163312243 Pa +wellControls1: Total rate: -979.5821480154148 mol/s; total surface volumetric rate: -23.148148148082612 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148082612 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.332 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.7211e+06, 9.43341e+06, 9.66441e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.58508e+06, -1.69347e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3836e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.57539e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02606e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3836e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.35976e+12, 2.38387e+10 } } mol +Time: 4.86e+08 s, dt: 4320000 s, Cycle: 123 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-03 ) ( Rwell ) = ( 3.49e-10 ) ( R ) = ( 3.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00232287 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581809 s | Solve Time: 0.331547 s + compositionalMultiphaseFlow: Max pressure change: 22421.698 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.120 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.634495294666749e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-03 ) ( Rwell ) = ( 7.56e-07 ) ( R ) = ( 2.63e-03 ) + Last LinSolve(iter,res) = ( 4, 2.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0015361 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582455 s | Solve Time: 0.331689 s + compositionalMultiphaseFlow: Max pressure change: 16.652 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.089 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6345607889434177e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-06 ) ( Rwell ) = ( 3.64e-11 ) ( R ) = ( 1.19e-06 ) + Last LinSolve(iter,res) = ( 4, 1.54e-03 ) +wellControls1: BHP (at the specified reference elevation): 2122242.8987974366 Pa +wellControls1: Total rate: -979.5821495892255 mol/s; total surface volumetric rate: -23.14814814809675 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814809675 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.334 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.69866e+06, 9.41705e+06, 9.64762e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.60749e+06, -1.70928e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37936e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.56905e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02246e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37936e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.35557e+12, 2.37964e+10 } } mol +Time: 4.91e+08 s, dt: 4320000 s, Cycle: 124 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-03 ) ( Rwell ) = ( 3.30e-10 ) ( R ) = ( 3.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00246123 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58557 s | Solve Time: 0.331244 s + compositionalMultiphaseFlow: Max pressure change: 22450.651 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.129 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6582087469796392e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-03 ) ( Rwell ) = ( 7.77e-07 ) ( R ) = ( 2.71e-03 ) + Last LinSolve(iter,res) = ( 4, 2.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00169899 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580986 s | Solve Time: 0.331376 s + compositionalMultiphaseFlow: Max pressure change: 16.308 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.091 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6581730621911817e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-06 ) ( Rwell ) = ( 3.93e-11 ) ( R ) = ( 1.32e-06 ) + Last LinSolve(iter,res) = ( 4, 1.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 2083043.0091242183 Pa +wellControls1: Total rate: -979.5821503532203 mol/s; total surface volumetric rate: -23.148148148082832 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.148148148082832 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.67619e+06, 9.40068e+06, 9.63082e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.62993e+06, -1.72508e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37513e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5627e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01886e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37513e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.35138e+12, 2.37541e+10 } } mol +Time: 4.95e+08 s, dt: 4320000 s, Cycle: 125 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.45e-03 ) ( Rwell ) = ( 3.39e-10 ) ( R ) = ( 3.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00248121 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579677 s | Solve Time: 0.331586 s + compositionalMultiphaseFlow: Max pressure change: 22477.895 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.138 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6802035740504095e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.72e-03 ) ( Rwell ) = ( 7.99e-07 ) ( R ) = ( 2.72e-03 ) + Last LinSolve(iter,res) = ( 4, 2.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00175496 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580854 s | Solve Time: 0.331222 s + compositionalMultiphaseFlow: Max pressure change: 17.865 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.086 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6802087121625675e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-06 ) ( Rwell ) = ( 6.11e-11 ) ( R ) = ( 1.32e-06 ) + Last LinSolve(iter,res) = ( 4, 1.75e-03 ) +wellControls1: BHP (at the specified reference elevation): 2043681.6974462655 Pa +wellControls1: Total rate: -979.5821508107695 mol/s; total surface volumetric rate: -23.14814814822798 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814822798 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.337 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.6537e+06, 9.38431e+06, 9.61403e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.6524e+06, -1.74089e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3709e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.55635e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01527e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3709e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.34719e+12, 2.37119e+10 } } mol +Time: 4.99e+08 s, dt: 4320000 s, Cycle: 126 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.47e-03 ) ( Rwell ) = ( 3.69e-10 ) ( R ) = ( 3.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00253314 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58071 s | Solve Time: 0.331163 s + compositionalMultiphaseFlow: Max pressure change: 22506.378 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.146 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7051522716027279e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.74e-03 ) ( Rwell ) = ( 8.22e-07 ) ( R ) = ( 2.74e-03 ) + Last LinSolve(iter,res) = ( 4, 2.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00187935 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583884 s | Solve Time: 0.331287 s + compositionalMultiphaseFlow: Max pressure change: 18.385 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.088 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7052047918131308e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-06 ) ( Rwell ) = ( 8.58e-11 ) ( R ) = ( 1.36e-06 ) + Last LinSolve(iter,res) = ( 4, 1.88e-03 ) +wellControls1: BHP (at the specified reference elevation): 2004157.0767887454 Pa +wellControls1: Total rate: -979.582151158116 mol/s; total surface volumetric rate: -23.14814814821373 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.14814814821373 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.339 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.63117e+06, 9.36794e+06, 9.59724e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.67489e+06, -1.75669e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.36667e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.55e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01167e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.36667e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.343e+12, 2.36696e+10 } } mol +Time: 5.04e+08 s, dt: 1320000 s, Cycle: 127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 4.01e-10 ) ( R ) = ( 1.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00619192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581925 s | Solve Time: 0.253725 s + compositionalMultiphaseFlow: Max pressure change: 6870.774 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.220 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4511059465149856e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 +***** INFO +***** LOCATION: /data/pau901/VDG_GSI/MelvinREY/WorkEnv/GEOSX_repos/GEOS_xmlErrors4/src/coreComponents/physicsSolvers/fluidFlow/wells/CompositionalMultiphaseWell.cpp:1678 +***** Controlling expression: this->getLogLevel() >= 1 +Control switch for well wellRegion1UniqueSubRegion from rate constraint to BHP constraint + ( Rflow ) = ( 5.25e-04 ) ( Rwell ) = ( 3.95e-03 ) ( R ) = ( 3.99e-03 ) + Last LinSolve(iter,res) = ( 3, 6.19e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0882458822969454e-08 + Line search @ 0.500: ( Rflow ) = ( 5.60e-04 ) ( Rwell ) = ( 9.38e-04 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.719683811491791e-09 + Line search @ 0.250: ( Rflow ) = ( 8.16e-04 ) ( Rwell ) = ( 5.70e-04 ) ( R ) = ( 9.96e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00583589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582898 s | Solve Time: 0.252092 s + compositionalMultiphaseFlow: Max pressure change: 3850.590 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.250 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7284377262782868e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.34e-05 ) ( Rwell ) = ( 1.15e-08 ) ( R ) = ( 8.34e-05 ) + Last LinSolve(iter,res) = ( 3, 5.84e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.989731541 Pa +wellControls1: Total rate: -978.7950797402708 mol/s; total surface volumetric rate: -23.129548738311453 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.129548738311453 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.62663e+06, 9.36294e+06, 9.59211e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.69742e+06, -1.77249e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.36538e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.54807e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01057e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.36538e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.34172e+12, 2.36567e+10 } } mol +Time: 5.05e+08 s, dt: 2640000 s, Cycle: 128 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 1.14e-08 ) ( R ) = ( 1.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00892775 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581009 s | Solve Time: 0.252373 s + compositionalMultiphaseFlow: Max pressure change: 10265.347 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.447 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0883057677268937e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.80e-04 ) ( Rwell ) = ( 1.00e-07 ) ( R ) = ( 9.80e-04 ) + Last LinSolve(iter,res) = ( 3, 8.93e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000011239 Pa +wellControls1: Total rate: -976.4411939425073 mol/s; total surface volumetric rate: -23.073924182889705 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -23.073924182889705 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.62011e+06, 9.35297e+06, 9.58185e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.70196e+06, -1.77732e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3628e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5442e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00838e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3628e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.33917e+12, 2.3631e+10 } } mol +Time: 5.08e+08 s, dt: 4320000 s, Cycle: 129 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.26e-03 ) ( Rwell ) = ( 1.00e-07 ) ( R ) = ( 3.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0052726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586053 s | Solve Time: 0.331661 s + compositionalMultiphaseFlow: Max pressure change: 16753.277 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.427 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1079314849181685e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.04e-03 ) ( Rwell ) = ( 2.62e-07 ) ( R ) = ( 3.04e-03 ) + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00197735 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581427 s | Solve Time: 0.33227 s + compositionalMultiphaseFlow: Max pressure change: 14.317 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.139 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.4508957469370216e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.96e-06 ) ( Rwell ) = ( 5.50e-10 ) ( R ) = ( 3.96e-06 ) + Last LinSolve(iter,res) = ( 4, 1.98e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000011844 Pa +wellControls1: Total rate: -972.6426916553023 mol/s; total surface volumetric rate: -22.98416451177492 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.98416451177492 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.60958e+06, 9.33672e+06, 9.5651e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.70848e+06, -1.78697e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3586e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5379e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00481e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3586e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.33501e+12, 2.35891e+10 } } mol +Time: 5.12e+08 s, dt: 4320000 s, Cycle: 130 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-03 ) ( Rwell ) = ( 5.50e-10 ) ( R ) = ( 1.80e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00494869 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58275 s | Solve Time: 0.333929 s + compositionalMultiphaseFlow: Max pressure change: 16701.060 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.416 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2723249998589665e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-03 ) ( Rwell ) = ( 2.59e-07 ) ( R ) = ( 2.76e-03 ) + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.457661174570802e-08 + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ( Rwell ) = ( 6.50e-08 ) ( R ) = ( 9.52e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00507244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581785 s | Solve Time: 0.330935 s + compositionalMultiphaseFlow: Max pressure change: 8349.795 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.672 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7779446803700694e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 6.49e-08 ) ( R ) = ( 1.44e-03 ) + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.873864479724375e-09 + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 4.87e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.791067459957276e-10 + Line search @ 0.250: ( Rflow ) = ( 7.93e-04 ) ( Rwell ) = ( 5.28e-08 ) ( R ) = ( 7.93e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00530379 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585356 s | Solve Time: 0.331252 s + compositionalMultiphaseFlow: Max pressure change: 6262.738 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.017 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5366321548526685e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 3.65e-08 ) ( R ) = ( 1.17e-03 ) + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.854582705415282e-10 + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ( Rwell ) = ( 3.55e-08 ) ( R ) = ( 9.79e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.704239385868505e-10 + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ( Rwell ) = ( 4.19e-08 ) ( R ) = ( 8.86e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.905425037866507e-10 + Line search @ 0.125: ( Rflow ) = ( 8.40e-04 ) ( Rwell ) = ( 4.67e-08 ) ( R ) = ( 8.40e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.5907365969478633e-10 + Line search @ 0.062: ( Rflow ) = ( 8.16e-04 ) ( Rwell ) = ( 4.96e-08 ) ( R ) = ( 8.16e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00505435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584349 s | Solve Time: 0.331696 s + compositionalMultiphaseFlow: Max pressure change: 5871.327 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.891 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4796284197871046e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.53e-04 ) ( Rwell ) = ( 3.21e-08 ) ( R ) = ( 9.53e-04 ) + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999649 Pa +wellControls1: Total rate: -968.8766137514534 mol/s; total surface volumetric rate: -22.895168870421372 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.895168870421372 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.59911e+06, 9.32053e+06, 9.5484e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.71901e+06, -1.80276e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35441e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.53162e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00125e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35441e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.33086e+12, 2.35474e+10 } } mol +Time: 5.16e+08 s, dt: 4320000 s, Cycle: 131 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-03 ) ( Rwell ) = ( 3.21e-08 ) ( R ) = ( 1.80e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00489732 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582745 s | Solve Time: 0.332488 s + compositionalMultiphaseFlow: Max pressure change: 16635.988 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.386 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.924925124325739e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-03 ) ( Rwell ) = ( 2.56e-07 ) ( R ) = ( 2.56e-03 ) + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.317078839908504e-08 + Line search @ 0.500: ( Rflow ) = ( 9.69e-04 ) ( Rwell ) = ( 8.01e-08 ) ( R ) = ( 9.69e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00565402 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582696 s | Solve Time: 0.331102 s + compositionalMultiphaseFlow: Max pressure change: 8318.921 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.672 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6499597244035158e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-03 ) ( Rwell ) = ( 6.42e-08 ) ( R ) = ( 1.83e-03 ) + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5018886134754439e-09 + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ( Rwell ) = ( 5.61e-08 ) ( R ) = ( 1.39e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.948362134082345e-10 + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 6.41e-08 ) ( R ) = ( 1.17e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.333127604094216e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 7.11e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.755612653146613e-10 + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 7.53e-08 ) ( R ) = ( 1.00e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00504755 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583345 s | Solve Time: 0.331198 s + compositionalMultiphaseFlow: Max pressure change: 7798.959 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.496 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8115966504694825e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 5.64e-08 ) ( R ) = ( 1.27e-03 ) + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2212890698748424e-09 + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 5.18e-08 ) ( R ) = ( 1.14e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.852020310674448e-10 + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 6.00e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.91097973187982e-10 + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 6.68e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.451155082880632e-10 + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 7.09e-08 ) ( R ) = ( 1.02e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0050697 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586288 s | Solve Time: 0.331137 s + compositionalMultiphaseFlow: Max pressure change: 7311.640 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.342 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.173436541852425e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 4.96e-08 ) ( R ) = ( 1.20e-03 ) + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.553078328394804e-10 + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 4.78e-08 ) ( R ) = ( 1.11e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0143950124330559e-09 + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.62e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.598695089290231e-10 + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 6.28e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.180549322858496e-10 + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 6.66e-08 ) ( R ) = ( 1.03e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00531126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580754 s | Solve Time: 0.330477 s + compositionalMultiphaseFlow: Max pressure change: 6855.717 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.206 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5435873407531062e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.31e-03 ) ( Rwell ) = ( 4.36e-08 ) ( R ) = ( 1.31e-03 ) + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.115767974852361e-10 + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 4.42e-08 ) ( R ) = ( 1.17e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0480974976800894e-09 + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 5.27e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.327031286725628e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.90e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.934754826990684e-10 + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 6.26e-08 ) ( R ) = ( 1.05e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00511814 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586205 s | Solve Time: 0.331348 s + compositionalMultiphaseFlow: Max pressure change: 6427.754 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.066 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.723508862878532e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 3.83e-08 ) ( R ) = ( 1.13e-03 ) + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.141511826347369e-10 + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 4.09e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.048781728130166e-09 + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 4.94e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.99906030302111e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.54e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.687988885976324e-10 + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 5.89e-08 ) ( R ) = ( 1.05e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00532646 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583594 s | Solve Time: 0.331274 s + compositionalMultiphaseFlow: Max pressure change: 6025.606 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.932 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.890942818467579e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 3.37e-08 ) ( R ) = ( 1.14e-03 ) + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.318530143545331e-10 + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 3.79e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.04717778892649e-09 + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 4.63e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.665789114597032e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.20e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.440101619707093e-10 + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.53e-08 ) ( R ) = ( 1.06e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0050903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585351 s | Solve Time: 0.331648 s + compositionalMultiphaseFlow: Max pressure change: 5649.037 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.812 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.946911825674192e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.36e-04 ) ( Rwell ) = ( 2.97e-08 ) ( R ) = ( 9.36e-04 ) + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000003576 Pa +wellControls1: Total rate: -965.1377113526753 mol/s; total surface volumetric rate: -22.80681618206437 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.80681618206437 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.174 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.5887e+06, 9.3044e+06, 9.53176e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.72948e+06, -1.81853e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35024e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.52536e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99771e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35024e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.32674e+12, 2.35058e+10 } } mol +Time: 5.21e+08 s, dt: 4320000 s, Cycle: 132 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-03 ) ( Rwell ) = ( 2.97e-08 ) ( R ) = ( 1.80e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0048938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587653 s | Solve Time: 0.33165 s + compositionalMultiphaseFlow: Max pressure change: 16567.387 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.363 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9476579066489705e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-03 ) ( Rwell ) = ( 2.54e-07 ) ( R ) = ( 2.57e-03 ) + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3273707183690817e-08 + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ( Rwell ) = ( 7.82e-08 ) ( R ) = ( 9.66e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00527929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585531 s | Solve Time: 0.330773 s + compositionalMultiphaseFlow: Max pressure change: 8284.530 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.651 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3724255065739044e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ( Rwell ) = ( 6.36e-08 ) ( R ) = ( 1.55e-03 ) + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6805479230441733e-09 + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 5.50e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.354277352713325e-10 + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 6.27e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.110869836348456e-10 + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 6.95e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.663176594339348e-10 + Line search @ 0.062: ( Rflow ) = ( 9.84e-04 ) ( Rwell ) = ( 7.36e-08 ) ( R ) = ( 9.84e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00528691 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579821 s | Solve Time: 0.331836 s + compositionalMultiphaseFlow: Max pressure change: 7767.039 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.486 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8204621143880217e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-03 ) ( Rwell ) = ( 5.59e-08 ) ( R ) = ( 1.46e-03 ) + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1879154326877028e-09 + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 5.08e-08 ) ( R ) = ( 1.22e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.80175163256547e-10 + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 5.87e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.831630982086836e-10 + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 6.53e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.397933211526151e-10 + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 6.92e-08 ) ( R ) = ( 1.01e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00509717 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582902 s | Solve Time: 0.331693 s + compositionalMultiphaseFlow: Max pressure change: 7282.633 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.340 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1327033472573476e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 4.91e-08 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.531089251169078e-10 + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 4.69e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.000836635789426e-09 + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 5.50e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.50566728161084e-10 + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 6.13e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.127726021569856e-10 + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 6.51e-08 ) ( R ) = ( 1.03e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00530694 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581629 s | Solve Time: 0.331576 s + compositionalMultiphaseFlow: Max pressure change: 6826.969 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.187 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4073949500547087e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 4.32e-08 ) ( R ) = ( 1.29e-03 ) + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.432341408986076e-10 + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 4.33e-08 ) ( R ) = ( 1.16e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0142245931987759e-09 + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 5.15e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.159007913732808e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.76e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.851083978962833e-10 + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 6.12e-08 ) ( R ) = ( 1.05e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00531304 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583654 s | Solve Time: 0.332395 s + compositionalMultiphaseFlow: Max pressure change: 6400.524 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.051 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6460552637885826e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 3.80e-08 ) ( R ) = ( 1.21e-03 ) + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.998296304099426e-10 + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 4.01e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0270853056937312e-09 + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 4.83e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.873127705337879e-10 + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 5.41e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.620660520870956e-10 + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.75e-08 ) ( R ) = ( 1.06e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00510938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584208 s | Solve Time: 0.331516 s + compositionalMultiphaseFlow: Max pressure change: 6001.326 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.931 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.769202200880727e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 3.34e-08 ) ( R ) = ( 1.06e-03 ) + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.566990284895269e-10 + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 3.71e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0180579712582016e-09 + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 4.52e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.530076562289878e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.08e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.3747150346717945e-10 + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.41e-08 ) ( R ) = ( 1.06e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00511685 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580938 s | Solve Time: 0.331224 s + compositionalMultiphaseFlow: Max pressure change: 5626.413 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.810 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.88713319918088e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.95e-04 ) ( Rwell ) = ( 2.94e-08 ) ( R ) = ( 9.95e-04 ) + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999999339 Pa +wellControls1: Total rate: -961.4239801110751 mol/s; total surface volumetric rate: -22.71905832642368 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.71905832642368 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.174 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.57835e+06, 9.28833e+06, 9.5152e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.73989e+06, -1.83428e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.34609e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.51913e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99418e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.34609e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.32262e+12, 2.34644e+10 } } mol +Time: 5.25e+08 s, dt: 4320000 s, Cycle: 133 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.79e-03 ) ( Rwell ) = ( 2.94e-08 ) ( R ) = ( 1.79e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00515145 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586599 s | Solve Time: 0.330791 s + compositionalMultiphaseFlow: Max pressure change: 16496.218 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.338 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9020414515912307e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-03 ) ( Rwell ) = ( 2.51e-07 ) ( R ) = ( 2.97e-03 ) + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.292906153833485e-08 + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ( Rwell ) = ( 7.75e-08 ) ( R ) = ( 1.18e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00506823 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584187 s | Solve Time: 0.331025 s + compositionalMultiphaseFlow: Max pressure change: 8249.392 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.650 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.263908089299548e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ( Rwell ) = ( 6.30e-08 ) ( R ) = ( 1.45e-03 ) + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.861336196284924e-09 + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ( Rwell ) = ( 5.45e-08 ) ( R ) = ( 1.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.727287781340465e-10 + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 6.21e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.866601897139503e-10 + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 6.88e-08 ) ( R ) = ( 1.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.558341564793068e-10 + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 7.29e-08 ) ( R ) = ( 1.20e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00507574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584579 s | Solve Time: 0.331716 s + compositionalMultiphaseFlow: Max pressure change: 7734.042 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.484 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5539618480886475e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.36e-03 ) ( Rwell ) = ( 5.54e-08 ) ( R ) = ( 1.36e-03 ) + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.352847722735362e-09 + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 5.03e-08 ) ( R ) = ( 1.28e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.214718987848869e-10 + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 5.82e-08 ) ( R ) = ( 1.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.597511591545981e-10 + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 6.47e-08 ) ( R ) = ( 1.22e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.295717198094962e-10 + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 6.86e-08 ) ( R ) = ( 1.21e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00529931 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5858 s | Solve Time: 0.332335 s + compositionalMultiphaseFlow: Max pressure change: 7250.546 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.332 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9744016421796573e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ( Rwell ) = ( 4.87e-08 ) ( R ) = ( 1.40e-03 ) + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0439871189760197e-09 + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 4.65e-08 ) ( R ) = ( 1.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.622855845492495e-10 + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 5.45e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.320623079427492e-10 + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 6.08e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.037141814767665e-10 + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 6.45e-08 ) ( R ) = ( 1.22e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00531753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583369 s | Solve Time: 0.331431 s + compositionalMultiphaseFlow: Max pressure change: 6797.071 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.178 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2646103881029944e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 4.28e-08 ) ( R ) = ( 1.30e-03 ) + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.58140225545867e-10 + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 4.29e-08 ) ( R ) = ( 1.26e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.824153712756356e-10 + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 5.10e-08 ) ( R ) = ( 1.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.02911070962864e-10 + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 5.71e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.793425656401951e-10 + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 6.06e-08 ) ( R ) = ( 1.22e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00531066 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582997 s | Solve Time: 0.331784 s + compositionalMultiphaseFlow: Max pressure change: 6372.646 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.042 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4879348581308136e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 3.77e-08 ) ( R ) = ( 1.21e-03 ) + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00181303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583617 s | Solve Time: 0.331585 s + compositionalMultiphaseFlow: Max pressure change: 5.289 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.054 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.854698725826779e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-06 ) ( Rwell ) = ( 1.53e-10 ) ( R ) = ( 1.16e-06 ) + Last LinSolve(iter,res) = ( 4, 1.81e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000001346 Pa +wellControls1: Total rate: -957.7332895440694 mol/s; total surface volumetric rate: -22.631846022616948 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.631846022616948 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.173 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.56804e+06, 9.27233e+06, 9.4987e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.75024e+06, -1.84999e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.34195e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.51293e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99066e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.34195e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.31853e+12, 2.34231e+10 } } mol +Time: 5.29e+08 s, dt: 4320000 s, Cycle: 134 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.78e-03 ) ( Rwell ) = ( 1.54e-10 ) ( R ) = ( 1.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00484084 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582693 s | Solve Time: 0.331628 s + compositionalMultiphaseFlow: Max pressure change: 16425.353 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.315 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.239575296909436e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-03 ) ( Rwell ) = ( 2.49e-07 ) ( R ) = ( 2.52e-03 ) + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4317185154387744e-08 + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ( Rwell ) = ( 6.23e-08 ) ( R ) = ( 9.31e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00565994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581695 s | Solve Time: 0.331911 s + compositionalMultiphaseFlow: Max pressure change: 8211.620 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.639 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4443168883104818e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-03 ) ( Rwell ) = ( 6.24e-08 ) ( R ) = ( 1.87e-03 ) + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.579916391631798e-09 + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 4.68e-08 ) ( R ) = ( 1.17e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.711407847717396e-10 + Line search @ 0.250: ( Rflow ) = ( 8.19e-04 ) ( Rwell ) = ( 5.06e-08 ) ( R ) = ( 8.19e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00527579 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580925 s | Solve Time: 0.331407 s + compositionalMultiphaseFlow: Max pressure change: 6160.575 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.984 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3431249445972071e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 3.51e-08 ) ( R ) = ( 1.19e-03 ) + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.028872094418716e-10 + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 3.41e-08 ) ( R ) = ( 1.00e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.678581021546393e-10 + Line search @ 0.250: ( Rflow ) = ( 9.10e-04 ) ( Rwell ) = ( 4.02e-08 ) ( R ) = ( 9.10e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.826249482865364e-10 + Line search @ 0.125: ( Rflow ) = ( 8.65e-04 ) ( Rwell ) = ( 4.49e-08 ) ( R ) = ( 8.65e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.534578185693249e-10 + Line search @ 0.062: ( Rflow ) = ( 8.42e-04 ) ( Rwell ) = ( 4.76e-08 ) ( R ) = ( 8.42e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00527801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590185 s | Solve Time: 0.331307 s + compositionalMultiphaseFlow: Max pressure change: 5775.385 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.852 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5227253902239113e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 3.09e-08 ) ( R ) = ( 1.09e-03 ) + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.738891749653476e-10 + Line search @ 0.500: ( Rflow ) = ( 9.67e-04 ) ( Rwell ) = ( 3.15e-08 ) ( R ) = ( 9.67e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.758725801248033e-10 + Line search @ 0.250: ( Rflow ) = ( 9.04e-04 ) ( Rwell ) = ( 3.76e-08 ) ( R ) = ( 9.04e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.590301555002952e-10 + Line search @ 0.125: ( Rflow ) = ( 8.73e-04 ) ( Rwell ) = ( 4.21e-08 ) ( R ) = ( 8.73e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.347648824814087e-10 + Line search @ 0.062: ( Rflow ) = ( 8.57e-04 ) ( Rwell ) = ( 4.48e-08 ) ( R ) = ( 8.57e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00504094 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581433 s | Solve Time: 0.331621 s + compositionalMultiphaseFlow: Max pressure change: 5414.444 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.737 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6308229211503544e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.99e-04 ) ( Rwell ) = ( 2.72e-08 ) ( R ) = ( 8.99e-04 ) + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999788 Pa +wellControls1: Total rate: -954.0665768343794 mol/s; total surface volumetric rate: -22.54519839890963 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.54519839890963 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.173 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.55777e+06, 9.25639e+06, 9.48228e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.76055e+06, -1.86566e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33783e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.50675e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98716e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33783e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.31445e+12, 2.3382e+10 } } mol +Time: 5.34e+08 s, dt: 3000000 s, Cycle: 135 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 2.72e-08 ) ( R ) = ( 1.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00356473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580636 s | Solve Time: 0.331563 s + compositionalMultiphaseFlow: Max pressure change: 11370.853 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.659 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2343232547173955e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-03 ) ( Rwell ) = ( 1.20e-07 ) ( R ) = ( 2.07e-03 ) + Last LinSolve(iter,res) = ( 4, 3.56e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0321182797312645e-08 + Line search @ 0.500: ( Rflow ) = ( 7.91e-04 ) ( Rwell ) = ( 4.35e-08 ) ( R ) = ( 7.91e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00950241 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584305 s | Solve Time: 0.252595 s + compositionalMultiphaseFlow: Max pressure change: 5686.793 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.906 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9219215935682996e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.50e-04 ) ( Rwell ) = ( 3.00e-08 ) ( R ) = ( 8.50e-04 ) + Last LinSolve(iter,res) = ( 3, 9.50e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000002107 Pa +wellControls1: Total rate: -951.5309178720926 mol/s; total surface volumetric rate: -22.48527931279708 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.48527931279708 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.120 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.55066e+06, 9.24534e+06, 9.47091e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.77082e+06, -1.88129e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33498e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.50246e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98473e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33498e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.31162e+12, 2.33535e+10 } } mol +Time: 5.37e+08 s, dt: 4320000 s, Cycle: 136 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.81e-03 ) ( Rwell ) = ( 3.00e-08 ) ( R ) = ( 2.81e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00470551 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583902 s | Solve Time: 0.331717 s + compositionalMultiphaseFlow: Max pressure change: 16302.838 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.280 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8826449116614583e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.42e-03 ) ( Rwell ) = ( 2.46e-07 ) ( R ) = ( 2.42e-03 ) + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00196415 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583367 s | Solve Time: 0.332018 s + compositionalMultiphaseFlow: Max pressure change: 12.003 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.123 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.352706290371543e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.62e-06 ) ( Rwell ) = ( 5.20e-10 ) ( R ) = ( 3.62e-06 ) + Last LinSolve(iter,res) = ( 4, 1.96e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000029623 Pa +wellControls1: Total rate: -947.9009402843338 mol/s; total surface volumetric rate: -22.39950154900022 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.39950154900022 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.54047e+06, 9.2295e+06, 9.4546e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.77793e+06, -1.89212e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33088e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.49632e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98125e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33088e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.30757e+12, 2.33127e+10 } } mol +Time: 5.41e+08 s, dt: 4320000 s, Cycle: 137 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-03 ) ( Rwell ) = ( 5.20e-10 ) ( R ) = ( 1.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00451046 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583702 s | Solve Time: 0.331529 s + compositionalMultiphaseFlow: Max pressure change: 16234.391 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.252 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.242529611480194e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.26e-03 ) ( Rwell ) = ( 2.44e-07 ) ( R ) = ( 2.26e-03 ) + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.43494504559294e-08 + Line search @ 0.500: ( Rflow ) = ( 9.24e-04 ) ( Rwell ) = ( 6.12e-08 ) ( R ) = ( 9.24e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00473537 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584148 s | Solve Time: 0.331609 s + compositionalMultiphaseFlow: Max pressure change: 8117.217 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.599 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5803299779904023e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 6.10e-08 ) ( R ) = ( 1.23e-03 ) + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7589374118619503e-09 + Line search @ 0.500: ( Rflow ) = ( 7.86e-04 ) ( Rwell ) = ( 4.58e-08 ) ( R ) = ( 7.86e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00477077 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582965 s | Solve Time: 0.33048 s + compositionalMultiphaseFlow: Max pressure change: 4060.785 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.309 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.818574678682296e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.25e-04 ) ( Rwell ) = ( 1.54e-08 ) ( R ) = ( 6.25e-04 ) + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999994931 Pa +wellControls1: Total rate: -944.2929456501531 mol/s; total surface volumetric rate: -22.314241811745966 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.314241811745966 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.53031e+06, 9.21372e+06, 9.43837e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.78812e+06, -1.90767e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3268e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.4902e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97778e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3268e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.30353e+12, 2.3272e+10 } } mol +Time: 5.45e+08 s, dt: 4320000 s, Cycle: 138 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-03 ) ( Rwell ) = ( 1.54e-08 ) ( R ) = ( 1.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00493602 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581348 s | Solve Time: 0.331428 s + compositionalMultiphaseFlow: Max pressure change: 16166.951 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.240 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.016048488735379e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-03 ) ( Rwell ) = ( 2.42e-07 ) ( R ) = ( 2.81e-03 ) + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.326772863270321e-08 + Line search @ 0.500: ( Rflow ) = ( 9.49e-04 ) ( Rwell ) = ( 6.81e-08 ) ( R ) = ( 9.49e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00474353 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583422 s | Solve Time: 0.330945 s + compositionalMultiphaseFlow: Max pressure change: 8082.073 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.599 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.222122625321731e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 6.06e-08 ) ( R ) = ( 1.24e-03 ) + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.343824023753882e-09 + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 4.92e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.89675530626721e-10 + Line search @ 0.250: ( Rflow ) = ( 9.99e-04 ) ( Rwell ) = ( 5.48e-08 ) ( R ) = ( 9.99e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.347040753558076e-10 + Line search @ 0.125: ( Rflow ) = ( 9.60e-04 ) ( Rwell ) = ( 6.05e-08 ) ( R ) = ( 9.60e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.772522377294308e-10 + Line search @ 0.062: ( Rflow ) = ( 9.41e-04 ) ( Rwell ) = ( 6.40e-08 ) ( R ) = ( 9.41e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00476717 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583031 s | Solve Time: 0.331699 s + compositionalMultiphaseFlow: Max pressure change: 7576.666 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.437 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1696441593045392e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 5.33e-08 ) ( R ) = ( 1.17e-03 ) + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7878588609576695e-09 + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 4.53e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.645692884887922e-10 + Line search @ 0.250: ( Rflow ) = ( 9.97e-04 ) ( Rwell ) = ( 5.14e-08 ) ( R ) = ( 9.97e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.214698838353684e-10 + Line search @ 0.125: ( Rflow ) = ( 9.69e-04 ) ( Rwell ) = ( 5.69e-08 ) ( R ) = ( 9.69e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.579764345535864e-10 + Line search @ 0.062: ( Rflow ) = ( 9.55e-04 ) ( Rwell ) = ( 6.02e-08 ) ( R ) = ( 9.55e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00599511 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584806 s | Solve Time: 0.331004 s + compositionalMultiphaseFlow: Max pressure change: 7103.386 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.293 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3841475743348042e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ( Rwell ) = ( 4.68e-08 ) ( R ) = ( 1.88e-03 ) + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0483645063175118e-09 + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ( Rwell ) = ( 4.18e-08 ) ( R ) = ( 1.42e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.815479374784218e-10 + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 4.81e-08 ) ( R ) = ( 1.19e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.16855019788909e-10 + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 5.34e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.3990411313643563e-10 + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 5.67e-08 ) ( R ) = ( 1.01e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00476882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585496 s | Solve Time: 0.33252 s + compositionalMultiphaseFlow: Max pressure change: 6659.821 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.140 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3039497259725863e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 4.12e-08 ) ( R ) = ( 1.03e-03 ) + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1072304184622794e-09 + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 3.86e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.352252140435667e-10 + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 4.51e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.740661362414357e-10 + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 5.02e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.1360914693200357e-10 + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 5.33e-08 ) ( R ) = ( 1.01e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0050805 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580843 s | Solve Time: 0.331011 s + compositionalMultiphaseFlow: Max pressure change: 6244.723 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.002 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6703316507715726e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 3.62e-08 ) ( R ) = ( 1.14e-03 ) + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.649869709387303e-10 + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 3.57e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.754943354143506e-10 + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 4.22e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.557915321891983e-10 + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 4.72e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.94875798725991e-10 + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 5.01e-08 ) ( R ) = ( 1.02e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00500504 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583727 s | Solve Time: 0.331511 s + compositionalMultiphaseFlow: Max pressure change: 5853.764 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.881 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.825911311037487e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.81e-04 ) ( Rwell ) = ( 3.18e-08 ) ( R ) = ( 9.81e-04 ) + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.000000317 Pa +wellControls1: Total rate: -940.705817717855 mol/s; total surface volumetric rate: -22.22947534024139 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.22947534024139 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.5202e+06, 9.198e+06, 9.4222e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.79828e+06, -1.92318e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.32274e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.48411e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97433e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.32274e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.29951e+12, 2.32315e+10 } } mol +Time: 5.49e+08 s, dt: 4320000 s, Cycle: 139 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-03 ) ( Rwell ) = ( 3.18e-08 ) ( R ) = ( 1.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00453079 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585194 s | Solve Time: 0.331365 s + compositionalMultiphaseFlow: Max pressure change: 16097.316 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.208 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8542164520750646e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ( Rwell ) = ( 2.40e-07 ) ( R ) = ( 2.29e-03 ) + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2700676449716184e-08 + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ( Rwell ) = ( 7.59e-08 ) ( R ) = ( 9.48e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00475802 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580306 s | Solve Time: 0.331565 s + compositionalMultiphaseFlow: Max pressure change: 8049.201 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.577 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.539880001288907e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 6.01e-08 ) ( R ) = ( 1.24e-03 ) + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5778314210734834e-09 + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 5.30e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.72515956654263e-10 + Line search @ 0.250: ( Rflow ) = ( 9.43e-04 ) ( Rwell ) = ( 6.07e-08 ) ( R ) = ( 9.43e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00470399 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585681 s | Solve Time: 0.332022 s + compositionalMultiphaseFlow: Max pressure change: 6038.124 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.936 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3254879960864514e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.19e-04 ) ( Rwell ) = ( 3.39e-08 ) ( R ) = ( 9.19e-04 ) + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999998338 Pa +wellControls1: Total rate: -937.1393639840895 mol/s; total surface volumetric rate: -22.14519777305321 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.14519777305321 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.51013e+06, 9.18234e+06, 9.40611e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.80839e+06, -1.93863e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.31869e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.47803e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97089e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.31869e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.2955e+12, 2.31912e+10 } } mol +Time: 5.54e+08 s, dt: 4320000 s, Cycle: 140 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-03 ) ( Rwell ) = ( 3.39e-08 ) ( R ) = ( 1.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00462685 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585253 s | Solve Time: 0.331327 s + compositionalMultiphaseFlow: Max pressure change: 16031.047 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.189 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8166991405953468e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-03 ) ( Rwell ) = ( 2.38e-07 ) ( R ) = ( 2.37e-03 ) + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2506242869368975e-08 + Line search @ 0.500: ( Rflow ) = ( 9.47e-04 ) ( Rwell ) = ( 7.64e-08 ) ( R ) = ( 9.47e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00453072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583786 s | Solve Time: 0.331306 s + compositionalMultiphaseFlow: Max pressure change: 8016.462 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.566 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7063837010056204e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 5.97e-08 ) ( R ) = ( 1.13e-03 ) + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.507647673371082e-09 + Line search @ 0.500: ( Rflow ) = ( 9.91e-04 ) ( Rwell ) = ( 5.31e-08 ) ( R ) = ( 9.91e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0174077136326787e-09 + Line search @ 0.250: ( Rflow ) = ( 9.23e-04 ) ( Rwell ) = ( 6.11e-08 ) ( R ) = ( 9.23e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00479931 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587825 s | Solve Time: 0.331612 s + compositionalMultiphaseFlow: Max pressure change: 6013.119 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.928 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.4668382609126525e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.50e-04 ) ( Rwell ) = ( 3.36e-08 ) ( R ) = ( 9.50e-04 ) + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000002272 Pa +wellControls1: Total rate: -933.5934982862362 mol/s; total surface volumetric rate: -22.061406755441787 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -22.061406755441787 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.170 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.5001e+06, 9.16674e+06, 9.39008e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.81846e+06, -1.95403e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.31466e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.47198e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96746e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.31466e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.29151e+12, 2.31511e+10 } } mol +Time: 5.58e+08 s, dt: 4320000 s, Cycle: 141 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-03 ) ( Rwell ) = ( 3.36e-08 ) ( R ) = ( 1.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00462254 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586623 s | Solve Time: 0.33081 s + compositionalMultiphaseFlow: Max pressure change: 15965.415 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.168 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8150683673011656e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-03 ) ( Rwell ) = ( 2.36e-07 ) ( R ) = ( 2.37e-03 ) + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2487245954216917e-08 + Line search @ 0.500: ( Rflow ) = ( 9.44e-04 ) ( Rwell ) = ( 7.59e-08 ) ( R ) = ( 9.44e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00504796 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584704 s | Solve Time: 0.331085 s + compositionalMultiphaseFlow: Max pressure change: 7984.412 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.565 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8955115255181454e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ( Rwell ) = ( 5.92e-08 ) ( R ) = ( 1.46e-03 ) + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3696866973944566e-09 + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 5.27e-08 ) ( R ) = ( 1.17e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.053830023245439e-09 + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 6.06e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.61065560467489e-10 + Line search @ 0.125: ( Rflow ) = ( 9.48e-04 ) ( Rwell ) = ( 6.73e-08 ) ( R ) = ( 9.48e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.89006066142872e-10 + Line search @ 0.062: ( Rflow ) = ( 9.11e-04 ) ( Rwell ) = ( 7.13e-08 ) ( R ) = ( 9.11e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00477794 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584437 s | Solve Time: 0.331498 s + compositionalMultiphaseFlow: Max pressure change: 7484.398 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.396 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.191974157739196e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-03 ) ( Rwell ) = ( 5.20e-08 ) ( R ) = ( 1.18e-03 ) + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0743120837375386e-09 + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 4.87e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0672254191490538e-09 + Line search @ 0.250: ( Rflow ) = ( 9.78e-04 ) ( Rwell ) = ( 5.68e-08 ) ( R ) = ( 9.78e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.223585228923525e-10 + Line search @ 0.125: ( Rflow ) = ( 9.44e-04 ) ( Rwell ) = ( 6.32e-08 ) ( R ) = ( 9.44e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.583116191587578e-10 + Line search @ 0.062: ( Rflow ) = ( 9.28e-04 ) ( Rwell ) = ( 6.71e-08 ) ( R ) = ( 9.28e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00506284 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581389 s | Solve Time: 0.331367 s + compositionalMultiphaseFlow: Max pressure change: 7018.046 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.255 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.609835236810909e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 4.57e-08 ) ( R ) = ( 1.29e-03 ) + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.925458067603586e-10 + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 4.50e-08 ) ( R ) = ( 1.11e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.107498204255819e-09 + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 5.32e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.944704976698858e-10 + Line search @ 0.125: ( Rflow ) = ( 9.73e-04 ) ( Rwell ) = ( 5.94e-08 ) ( R ) = ( 9.73e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.32371480232996e-10 + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ( Rwell ) = ( 6.31e-08 ) ( R ) = ( 9.50e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00467823 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584018 s | Solve Time: 0.331752 s + compositionalMultiphaseFlow: Max pressure change: 6578.768 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.108 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7377654587823486e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 4.02e-08 ) ( R ) = ( 1.00e-03 ) + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.682290276671665e-10 + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ( Rwell ) = ( 4.16e-08 ) ( R ) = ( 9.76e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0923685289654372e-09 + Line search @ 0.250: ( Rflow ) = ( 9.63e-04 ) ( Rwell ) = ( 4.98e-08 ) ( R ) = ( 9.63e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.516636285094137e-10 + Line search @ 0.125: ( Rflow ) = ( 9.57e-04 ) ( Rwell ) = ( 5.58e-08 ) ( R ) = ( 9.57e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.02165087290507e-10 + Line search @ 0.062: ( Rflow ) = ( 9.53e-04 ) ( Rwell ) = ( 5.93e-08 ) ( R ) = ( 9.53e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00468481 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58398 s | Solve Time: 0.331218 s + compositionalMultiphaseFlow: Max pressure change: 6167.825 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.977 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9624264152872115e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.43e-04 ) ( Rwell ) = ( 3.54e-08 ) ( R ) = ( 9.43e-04 ) + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999997735 Pa +wellControls1: Total rate: -930.0679609474823 mol/s; total surface volumetric rate: -21.97809611961665 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.97809611961665 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.170 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.4901e+06, 9.1512e+06, 9.37411e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.8285e+06, -1.96938e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.31064e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.46596e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96404e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.31064e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.28753e+12, 2.31111e+10 } } mol +Time: 5.62e+08 s, dt: 4320000 s, Cycle: 142 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-03 ) ( Rwell ) = ( 3.54e-08 ) ( R ) = ( 1.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00451832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582323 s | Solve Time: 0.331909 s + compositionalMultiphaseFlow: Max pressure change: 15900.492 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.144 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.783378971749073e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ( Rwell ) = ( 2.34e-07 ) ( R ) = ( 2.29e-03 ) + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2319951553662065e-08 + Line search @ 0.500: ( Rflow ) = ( 9.43e-04 ) ( Rwell ) = ( 7.63e-08 ) ( R ) = ( 9.43e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00510066 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58537 s | Solve Time: 0.331582 s + compositionalMultiphaseFlow: Max pressure change: 7951.095 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.546 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0203413386710167e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ( Rwell ) = ( 5.87e-08 ) ( R ) = ( 1.45e-03 ) + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.302081442666747e-09 + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 5.28e-08 ) ( R ) = ( 1.14e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0837363229043717e-09 + Line search @ 0.250: ( Rflow ) = ( 9.86e-04 ) ( Rwell ) = ( 6.09e-08 ) ( R ) = ( 9.86e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.750480423065255e-10 + Line search @ 0.125: ( Rflow ) = ( 9.09e-04 ) ( Rwell ) = ( 6.77e-08 ) ( R ) = ( 9.09e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0050521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588073 s | Solve Time: 0.33129 s + compositionalMultiphaseFlow: Max pressure change: 6958.583 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.238 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8171666111020954e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 4.50e-08 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.154561387778813e-10 + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 4.51e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1550003176097334e-09 + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 5.36e-08 ) ( R ) = ( 1.00e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.149843105404898e-10 + Line search @ 0.125: ( Rflow ) = ( 9.56e-04 ) ( Rwell ) = ( 5.99e-08 ) ( R ) = ( 9.56e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.418200332840684e-10 + Line search @ 0.062: ( Rflow ) = ( 9.33e-04 ) ( Rwell ) = ( 6.36e-08 ) ( R ) = ( 9.33e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00477615 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583504 s | Solve Time: 0.332167 s + compositionalMultiphaseFlow: Max pressure change: 6523.060 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.090 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9656131994570956e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 3.96e-08 ) ( R ) = ( 1.04e-03 ) + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.077877090504558e-10 + Line search @ 0.500: ( Rflow ) = ( 9.83e-04 ) ( Rwell ) = ( 4.17e-08 ) ( R ) = ( 9.83e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.145386119283387e-09 + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ( Rwell ) = ( 5.02e-08 ) ( R ) = ( 9.58e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.752231162034718e-10 + Line search @ 0.125: ( Rflow ) = ( 9.45e-04 ) ( Rwell ) = ( 5.63e-08 ) ( R ) = ( 9.45e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.132078095826387e-10 + Line search @ 0.062: ( Rflow ) = ( 9.39e-04 ) ( Rwell ) = ( 5.98e-08 ) ( R ) = ( 9.39e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00468119 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583686 s | Solve Time: 0.331677 s + compositionalMultiphaseFlow: Max pressure change: 6115.577 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.960 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.1252204157894425e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.40e-04 ) ( Rwell ) = ( 3.48e-08 ) ( R ) = ( 9.40e-04 ) + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.000000693 Pa +wellControls1: Total rate: -926.5625767363072 mol/s; total surface volumetric rate: -21.89526173275676 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.89526173275676 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.170 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.48015e+06, 9.13572e+06, 9.35821e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.83849e+06, -1.98467e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30664e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.45995e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96064e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30664e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.28356e+12, 2.30712e+10 } } mol +Time: 5.67e+08 s, dt: 1320000 s, Cycle: 143 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-04 ) ( Rwell ) = ( 3.48e-08 ) ( R ) = ( 5.35e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00588006 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586214 s | Solve Time: 0.252405 s + compositionalMultiphaseFlow: Max pressure change: 4854.588 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.606 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.177768076983e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-04 ) ( Rwell ) = ( 2.19e-08 ) ( R ) = ( 1.34e-04 ) + Last LinSolve(iter,res) = ( 3, 5.88e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999997276 Pa +wellControls1: Total rate: -925.4933580716639 mol/s; total surface volumetric rate: -21.869995791801855 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.869995791801855 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.052 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.47711e+06, 9.13099e+06, 9.35336e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.84844e+06, -1.99992e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30541e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.45812e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9596e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30541e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.28236e+12, 2.30591e+10 } } mol +Time: 5.68e+08 s, dt: 2640000 s, Cycle: 144 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 2.19e-08 ) ( R ) = ( 1.08e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00926498 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582055 s | Solve Time: 0.252187 s + compositionalMultiphaseFlow: Max pressure change: 9681.190 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.253 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.393654520906125e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.37e-04 ) ( Rwell ) = ( 8.70e-08 ) ( R ) = ( 7.37e-04 ) + Last LinSolve(iter,res) = ( 3, 9.26e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000001404 Pa +wellControls1: Total rate: -923.362493764426 mol/s; total surface volumetric rate: -21.819641698369963 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.819641698369963 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.104 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.47104e+06, 9.12156e+06, 9.34368e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.85148e+06, -2.00457e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30298e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.45446e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95753e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30298e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.27994e+12, 2.30349e+10 } } mol +Time: 5.71e+08 s, dt: 4320000 s, Cycle: 145 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.77e-03 ) ( Rwell ) = ( 8.70e-08 ) ( R ) = ( 2.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00504359 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581708 s | Solve Time: 0.331309 s + compositionalMultiphaseFlow: Max pressure change: 15782.109 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.117 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0561869873425564e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.91e-03 ) ( Rwell ) = ( 2.31e-07 ) ( R ) = ( 2.91e-03 ) + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8659652267771776e-08 + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 1.01e-07 ) ( R ) = ( 1.01e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00478384 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582726 s | Solve Time: 0.332101 s + compositionalMultiphaseFlow: Max pressure change: 7893.840 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.539 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.233718791686215e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 5.80e-08 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0806040224030653e-09 + Line search @ 0.500: ( Rflow ) = ( 6.73e-04 ) ( Rwell ) = ( 6.51e-08 ) ( R ) = ( 6.73e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00509801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583032 s | Solve Time: 0.332121 s + compositionalMultiphaseFlow: Max pressure change: 3949.559 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.277 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.221724107608907e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.36e-04 ) ( Rwell ) = ( 1.48e-08 ) ( R ) = ( 7.36e-04 ) + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000003597 Pa +wellControls1: Total rate: -919.8961536002105 mol/s; total surface volumetric rate: -21.73773063953564 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.73773063953564 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.46116e+06, 9.10619e+06, 9.3279e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.85755e+06, -2.01385e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.299e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.4485e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95415e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.299e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.27601e+12, 2.29953e+10 } } mol +Time: 5.75e+08 s, dt: 4320000 s, Cycle: 146 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-03 ) ( Rwell ) = ( 1.48e-08 ) ( R ) = ( 1.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0045122 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58799 s | Solve Time: 0.331897 s + compositionalMultiphaseFlow: Max pressure change: 15717.024 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.084 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.040036944401692e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ( Rwell ) = ( 2.29e-07 ) ( R ) = ( 2.29e-03 ) + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3469753029914386e-08 + Line search @ 0.500: ( Rflow ) = ( 9.30e-04 ) ( Rwell ) = ( 6.45e-08 ) ( R ) = ( 9.30e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00487226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584597 s | Solve Time: 0.331261 s + compositionalMultiphaseFlow: Max pressure change: 7859.889 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.516 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.780251053470579e-10 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 5.74e-08 ) ( R ) = ( 1.33e-03 ) + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1050475806916324e-09 + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 4.66e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.652293160769318e-10 + Line search @ 0.250: ( Rflow ) = ( 8.88e-04 ) ( Rwell ) = ( 5.20e-08 ) ( R ) = ( 8.88e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00466477 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583903 s | Solve Time: 0.332832 s + compositionalMultiphaseFlow: Max pressure change: 5895.638 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.891 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.329344273022116e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.14e-04 ) ( Rwell ) = ( 3.24e-08 ) ( R ) = ( 9.14e-04 ) + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000002566 Pa +wellControls1: Total rate: -916.4483986967641 mol/s; total surface volumetric rate: -21.656257907238633 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.656257907238633 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.45132e+06, 9.09088e+06, 9.31218e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.86743e+06, -2.02899e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.29504e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.44257e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95079e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.29504e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.27209e+12, 2.29559e+10 } } mol +Time: 5.79e+08 s, dt: 4320000 s, Cycle: 147 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-03 ) ( Rwell ) = ( 3.24e-08 ) ( R ) = ( 1.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00481187 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582757 s | Solve Time: 0.331293 s + compositionalMultiphaseFlow: Max pressure change: 15655.692 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.065 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.749315919370332e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-03 ) ( Rwell ) = ( 2.27e-07 ) ( R ) = ( 2.55e-03 ) + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1980162023815808e-08 + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ( Rwell ) = ( 7.30e-08 ) ( R ) = ( 9.55e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00487103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584225 s | Solve Time: 0.331174 s + compositionalMultiphaseFlow: Max pressure change: 7829.101 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.512 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7297797638704537e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 5.70e-08 ) ( R ) = ( 1.33e-03 ) + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.438871133352393e-09 + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 5.08e-08 ) ( R ) = ( 1.14e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0089590274375837e-09 + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 5.83e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.360757724508062e-10 + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 6.48e-08 ) ( R ) = ( 1.00e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.758744592299081e-10 + Line search @ 0.062: ( Rflow ) = ( 9.78e-04 ) ( Rwell ) = ( 6.87e-08 ) ( R ) = ( 9.78e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00552234 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581834 s | Solve Time: 0.331472 s + compositionalMultiphaseFlow: Max pressure change: 7339.103 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.361 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.281938304982134e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-03 ) ( Rwell ) = ( 5.01e-08 ) ( R ) = ( 1.63e-03 ) + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.975450382919803e-10 + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 4.69e-08 ) ( R ) = ( 1.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0702306818544116e-09 + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 5.46e-08 ) ( R ) = ( 1.14e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.092803177068731e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 6.09e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.481305409560377e-10 + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 6.46e-08 ) ( R ) = ( 1.02e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00501166 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584587 s | Solve Time: 0.331735 s + compositionalMultiphaseFlow: Max pressure change: 6882.057 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.212 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.495859852125193e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 4.40e-08 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.503332399849683e-10 + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 4.33e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.072517630262837e-09 + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 5.12e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.721353639273843e-10 + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 5.72e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.19993825776055e-10 + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 6.07e-08 ) ( R ) = ( 1.03e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00553367 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582977 s | Solve Time: 0.331619 s + compositionalMultiphaseFlow: Max pressure change: 6450.889 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.076 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8025446408008747e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 3.87e-08 ) ( R ) = ( 1.44e-03 ) + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.445874944915886e-10 + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 4.00e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.093220847181442e-09 + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 4.80e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.40606251273357e-10 + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 5.37e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.937672493099399e-10 + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.71e-08 ) ( R ) = ( 1.06e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00521244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587484 s | Solve Time: 0.331272 s + compositionalMultiphaseFlow: Max pressure change: 6048.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.945 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9186160155347807e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 3.40e-08 ) ( R ) = ( 1.20e-03 ) + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.8951543646657e-10 + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 3.70e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0816484374842616e-09 + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 4.49e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.044506172311117e-10 + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 5.05e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.681024456942851e-10 + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 5.36e-08 ) ( R ) = ( 1.07e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00467319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58569 s | Solve Time: 0.331135 s + compositionalMultiphaseFlow: Max pressure change: 5670.574 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.817 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9746530794128034e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.88e-04 ) ( Rwell ) = ( 3.00e-08 ) ( R ) = ( 8.88e-04 ) + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999882 Pa +wellControls1: Total rate: -913.0202523764283 mol/s; total surface volumetric rate: -21.57524861817197 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.57524861817197 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.44151e+06, 9.07562e+06, 9.29653e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.87727e+06, -2.04408e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.2911e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.43665e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94743e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.2911e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.26818e+12, 2.29167e+10 } } mol +Time: 5.84e+08 s, dt: 4320000 s, Cycle: 148 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.73e-03 ) ( Rwell ) = ( 3.00e-08 ) ( R ) = ( 1.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00547306 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584821 s | Solve Time: 0.331207 s + compositionalMultiphaseFlow: Max pressure change: 15591.925 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.042 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.690917166869866e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-03 ) ( Rwell ) = ( 2.26e-07 ) ( R ) = ( 3.38e-03 ) + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1464886423849805e-08 + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ( Rwell ) = ( 7.13e-08 ) ( R ) = ( 1.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00462443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5851 s | Solve Time: 0.331206 s + compositionalMultiphaseFlow: Max pressure change: 7799.162 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.499 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2852966468912541e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 5.66e-08 ) ( R ) = ( 1.20e-03 ) + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00989839 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58339 s | Solve Time: 0.252064 s + compositionalMultiphaseFlow: Max pressure change: 5.167 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.059 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.376915688363852e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-06 ) ( Rwell ) = ( 1.95e-10 ) ( R ) = ( 1.85e-06 ) + Last LinSolve(iter,res) = ( 3, 9.90e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.000001492 Pa +wellControls1: Total rate: -909.6109181428774 mol/s; total surface volumetric rate: -21.4946847764805 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.4946847764805 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.43174e+06, 9.06042e+06, 9.28093e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.88708e+06, -2.05912e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28717e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.43075e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94409e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28717e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.26429e+12, 2.28775e+10 } } mol +Time: 5.88e+08 s, dt: 4320000 s, Cycle: 149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-03 ) ( Rwell ) = ( 1.95e-10 ) ( R ) = ( 1.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00577217 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582199 s | Solve Time: 0.331976 s + compositionalMultiphaseFlow: Max pressure change: 15532.806 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5.028 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9571629256430754e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-03 ) ( Rwell ) = ( 2.23e-07 ) ( R ) = ( 4.04e-03 ) + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2214850181612178e-08 + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 5.58e-08 ) ( R ) = ( 1.25e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0050263 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58441 s | Solve Time: 0.33169 s + compositionalMultiphaseFlow: Max pressure change: 7768.859 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.492 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3844821672724947e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-03 ) ( Rwell ) = ( 5.61e-08 ) ( R ) = ( 1.43e-03 ) + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.148010407905133e-09 + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ( Rwell ) = ( 4.19e-08 ) ( R ) = ( 1.34e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.817525184857118e-10 + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 4.53e-08 ) ( R ) = ( 1.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.958304877789033e-10 + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 4.97e-08 ) ( R ) = ( 1.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.546736238035919e-10 + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 5.25e-08 ) ( R ) = ( 1.26e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0045753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582723 s | Solve Time: 0.331238 s + compositionalMultiphaseFlow: Max pressure change: 7283.274 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.336 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.130251197662858e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 4.94e-08 ) ( R ) = ( 1.11e-03 ) + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00976223 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58686 s | Solve Time: 0.252583 s + compositionalMultiphaseFlow: Max pressure change: 4.816 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.054 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.22804291367163e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-06 ) ( Rwell ) = ( 2.07e-10 ) ( R ) = ( 1.65e-06 ) + Last LinSolve(iter,res) = ( 3, 9.76e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999991856 Pa +wellControls1: Total rate: -906.2210759973015 mol/s; total surface volumetric rate: -21.414580649348217 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.414580649348217 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.167 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.42201e+06, 9.04527e+06, 9.2654e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.89685e+06, -2.0741e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28326e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.42488e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94077e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28326e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.26042e+12, 2.28385e+10 } } mol +Time: 5.92e+08 s, dt: 4320000 s, Cycle: 150 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-03 ) ( Rwell ) = ( 2.07e-10 ) ( R ) = ( 1.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00523899 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587322 s | Solve Time: 0.331327 s + compositionalMultiphaseFlow: Max pressure change: 15474.960 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.996 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.014591720695847e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-03 ) ( Rwell ) = ( 2.22e-07 ) ( R ) = ( 3.36e-03 ) + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2626975293427165e-08 + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ( Rwell ) = ( 5.54e-08 ) ( R ) = ( 9.13e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0052184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580715 s | Solve Time: 0.331123 s + compositionalMultiphaseFlow: Max pressure change: 7736.600 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.481 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9663495276489584e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ( Rwell ) = ( 5.57e-08 ) ( R ) = ( 1.55e-03 ) + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9063573769860795e-09 + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 4.16e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.5353320271269695e-10 + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 4.50e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.212026366052669e-10 + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ( Rwell ) = ( 4.93e-08 ) ( R ) = ( 9.89e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.6444314233108344e-10 + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ( Rwell ) = ( 5.21e-08 ) ( R ) = ( 9.49e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00455294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583608 s | Solve Time: 0.332056 s + compositionalMultiphaseFlow: Max pressure change: 7254.503 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.327 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7388236406290503e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 4.90e-08 ) ( R ) = ( 1.10e-03 ) + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4585381508401838e-09 + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 3.83e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.8242287114798046e-10 + Line search @ 0.250: ( Rflow ) = ( 9.87e-04 ) ( Rwell ) = ( 4.21e-08 ) ( R ) = ( 9.87e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.080759146736114e-10 + Line search @ 0.125: ( Rflow ) = ( 9.68e-04 ) ( Rwell ) = ( 4.64e-08 ) ( R ) = ( 9.68e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.474788234925086e-10 + Line search @ 0.062: ( Rflow ) = ( 9.59e-04 ) ( Rwell ) = ( 4.90e-08 ) ( R ) = ( 9.59e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0047549 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583721 s | Solve Time: 0.331587 s + compositionalMultiphaseFlow: Max pressure change: 6801.810 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.190 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3367266182839899e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 4.30e-08 ) ( R ) = ( 1.16e-03 ) + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9286505725801817e-09 + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 3.53e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.91955468082017e-10 + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 3.95e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.018312432270022e-10 + Line search @ 0.125: ( Rflow ) = ( 9.83e-04 ) ( Rwell ) = ( 4.36e-08 ) ( R ) = ( 9.83e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3281843947463585e-10 + Line search @ 0.062: ( Rflow ) = ( 9.71e-04 ) ( Rwell ) = ( 4.61e-08 ) ( R ) = ( 9.71e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0055321 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582496 s | Solve Time: 0.331436 s + compositionalMultiphaseFlow: Max pressure change: 6375.148 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.046 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.137307359400097e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 3.78e-08 ) ( R ) = ( 1.44e-03 ) + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4343961574070363e-09 + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 3.25e-08 ) ( R ) = ( 1.20e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.263220887423813e-10 + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 3.70e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.98769248125086e-10 + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 4.10e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.207524246207072e-10 + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 4.34e-08 ) ( R ) = ( 1.00e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00524727 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580943 s | Solve Time: 0.331526 s + compositionalMultiphaseFlow: Max pressure change: 5976.621 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.918 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1409971856224388e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 3.33e-08 ) ( R ) = ( 1.21e-03 ) + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2569791874028624e-09 + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 3.00e-08 ) ( R ) = ( 1.11e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5175729823654365e-10 + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 3.46e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.818716536902912e-10 + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 3.85e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.049059893456274e-10 + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 4.08e-08 ) ( R ) = ( 1.01e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00469093 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584629 s | Solve Time: 0.331324 s + compositionalMultiphaseFlow: Max pressure change: 5604.014 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.799 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2121079695504022e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.95e-04 ) ( Rwell ) = ( 2.92e-08 ) ( R ) = ( 8.95e-04 ) + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999996475 Pa +wellControls1: Total rate: -902.8505450842824 mol/s; total surface volumetric rate: -21.334931901108515 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.334931901108515 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.167 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.41231e+06, 9.03019e+06, 9.24992e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.90658e+06, -2.08902e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27935e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.41903e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93745e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27935e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.25656e+12, 2.27997e+10 } } mol +Time: 5.97e+08 s, dt: 3000000 s, Cycle: 151 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 2.92e-08 ) ( R ) = ( 1.20e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00962375 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582287 s | Solve Time: 0.252441 s + compositionalMultiphaseFlow: Max pressure change: 10719.080 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.605 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.148130668315872e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-03 ) ( Rwell ) = ( 1.07e-07 ) ( R ) = ( 1.42e-03 ) + Last LinSolve(iter,res) = ( 3, 9.62e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.841547243816251e-09 + Line search @ 0.500: ( Rflow ) = ( 9.39e-04 ) ( Rwell ) = ( 4.13e-08 ) ( R ) = ( 9.39e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00965197 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587273 s | Solve Time: 0.252351 s + compositionalMultiphaseFlow: Max pressure change: 5360.544 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.748 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4621550354098076e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.92e-04 ) ( Rwell ) = ( 2.67e-08 ) ( R ) = ( 6.92e-04 ) + Last LinSolve(iter,res) = ( 3, 9.65e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.000000144 Pa +wellControls1: Total rate: -900.519019224533 mol/s; total surface volumetric rate: -21.2798364642754 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.2798364642754 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.40559e+06, 9.01973e+06, 9.2392e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.91628e+06, -2.1039e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27665e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.41498e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93516e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27665e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.25388e+12, 2.27728e+10 } } mol +Time: 6.00e+08 s, dt: 4320000 s, Cycle: 152 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-03 ) ( Rwell ) = ( 2.67e-08 ) ( R ) = ( 2.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00482466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583241 s | Solve Time: 0.33139 s + compositionalMultiphaseFlow: Max pressure change: 15372.879 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.983 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8101414528691748e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.69e-03 ) ( Rwell ) = ( 2.19e-07 ) ( R ) = ( 2.69e-03 ) + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2176474101520682e-08 + Line search @ 0.500: ( Rflow ) = ( 9.50e-04 ) ( Rwell ) = ( 6.82e-08 ) ( R ) = ( 9.50e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00494705 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58461 s | Solve Time: 0.331813 s + compositionalMultiphaseFlow: Max pressure change: 7689.938 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.461 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3513343777304954e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-03 ) ( Rwell ) = ( 5.50e-08 ) ( R ) = ( 1.41e-03 ) + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6634134070159234e-09 + Line search @ 0.500: ( Rflow ) = ( 7.45e-04 ) ( Rwell ) = ( 4.79e-08 ) ( R ) = ( 7.45e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00479634 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586229 s | Solve Time: 0.331416 s + compositionalMultiphaseFlow: Max pressure change: 3848.158 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.241 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.8673637342844245e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.40e-04 ) ( Rwell ) = ( 1.40e-08 ) ( R ) = ( 6.40e-04 ) + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999991225 Pa +wellControls1: Total rate: -897.1798869319109 mol/s; total surface volumetric rate: -21.200930929442748 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.200930929442748 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.166 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.39596e+06, 9.00474e+06, 9.22383e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.923e+06, -2.1142e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27278e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.40917e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93186e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27278e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.25004e+12, 2.27342e+10 } } mol +Time: 6.04e+08 s, dt: 4320000 s, Cycle: 153 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-03 ) ( Rwell ) = ( 1.40e-08 ) ( R ) = ( 1.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00524495 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58514 s | Solve Time: 0.331607 s + compositionalMultiphaseFlow: Max pressure change: 15314.617 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.951 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9275624924274268e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-03 ) ( Rwell ) = ( 2.18e-07 ) ( R ) = ( 3.16e-03 ) + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2603246274677247e-08 + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 6.13e-08 ) ( R ) = ( 1.14e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00469284 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587099 s | Solve Time: 0.331338 s + compositionalMultiphaseFlow: Max pressure change: 7660.337 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.455 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.830673969839609e-10 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 5.46e-08 ) ( R ) = ( 1.24e-03 ) + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2524103693299935e-09 + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 4.43e-08 ) ( R ) = ( 1.19e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.92929039200385e-10 + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 4.94e-08 ) ( R ) = ( 1.16e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.257618950262668e-10 + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 5.45e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.701450340149904e-10 + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 5.77e-08 ) ( R ) = ( 1.14e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00539777 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588273 s | Solve Time: 0.331203 s + compositionalMultiphaseFlow: Max pressure change: 7180.659 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.299 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.854753679761075e-10 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ( Rwell ) = ( 4.80e-08 ) ( R ) = ( 1.55e-03 ) + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6024197524444617e-09 + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 4.08e-08 ) ( R ) = ( 1.35e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.900215954175337e-10 + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 4.63e-08 ) ( R ) = ( 1.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.17422010687585e-10 + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 5.12e-08 ) ( R ) = ( 1.19e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.517641816192963e-10 + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 5.43e-08 ) ( R ) = ( 1.17e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00552324 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582688 s | Solve Time: 0.331422 s + compositionalMultiphaseFlow: Max pressure change: 6732.229 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.156 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1730105775598076e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.52e-03 ) ( Rwell ) = ( 4.22e-08 ) ( R ) = ( 1.52e-03 ) + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1685806766692508e-09 + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 3.77e-08 ) ( R ) = ( 1.35e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.323992523566858e-10 + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 4.34e-08 ) ( R ) = ( 1.26e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.950434672248207e-10 + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 4.82e-08 ) ( R ) = ( 1.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.2969194868902605e-10 + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 5.11e-08 ) ( R ) = ( 1.19e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00535825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580434 s | Solve Time: 0.332456 s + compositionalMultiphaseFlow: Max pressure change: 6311.936 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.022 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.427844176227211e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 3.71e-08 ) ( R ) = ( 1.35e-03 ) + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.201206463416156e-10 + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 3.48e-08 ) ( R ) = ( 1.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.488595299420808e-10 + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 4.06e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.679246045138143e-10 + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 4.53e-08 ) ( R ) = ( 1.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.073020809514105e-10 + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 4.80e-08 ) ( R ) = ( 1.20e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00472271 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585453 s | Solve Time: 0.331215 s + compositionalMultiphaseFlow: Max pressure change: 5918.231 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.899 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6198987706772527e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.72e-04 ) ( Rwell ) = ( 3.27e-08 ) ( R ) = ( 9.72e-04 ) + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000000054 Pa +wellControls1: Total rate: -893.8589755401247 mol/s; total surface volumetric rate: -21.122455515107514 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.122455515107514 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.166 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.38636e+06, 8.9898e+06, 9.20851e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.93263e+06, -2.12898e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26892e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.40337e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92858e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26892e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.24622e+12, 2.26958e+10 } } mol +Time: 6.08e+08 s, dt: 4320000 s, Cycle: 154 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.71e-03 ) ( Rwell ) = ( 3.27e-08 ) ( R ) = ( 1.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00471883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584392 s | Solve Time: 0.331076 s + compositionalMultiphaseFlow: Max pressure change: 15260.083 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.936 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6874072633908952e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-03 ) ( Rwell ) = ( 2.16e-07 ) ( R ) = ( 2.52e-03 ) + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1585201404050736e-08 + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ( Rwell ) = ( 7.04e-08 ) ( R ) = ( 9.79e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00531172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5808 s | Solve Time: 0.331029 s + compositionalMultiphaseFlow: Max pressure change: 7629.653 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.452 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.979616470748624e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ( Rwell ) = ( 5.42e-08 ) ( R ) = ( 1.60e-03 ) + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2446277342093026e-09 + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 4.87e-08 ) ( R ) = ( 1.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0540570638539748e-09 + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 5.62e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.456451177669578e-10 + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 6.24e-08 ) ( R ) = ( 1.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.774174471895321e-10 + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 6.62e-08 ) ( R ) = ( 1.02e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00537331 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581497 s | Solve Time: 0.330893 s + compositionalMultiphaseFlow: Max pressure change: 7153.182 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.299 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3800478254898394e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ( Rwell ) = ( 4.76e-08 ) ( R ) = ( 1.54e-03 ) + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.493962200262217e-10 + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 4.50e-08 ) ( R ) = ( 1.28e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0888884238724472e-09 + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 5.26e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.142339107981456e-10 + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 5.86e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.495151000900478e-10 + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 6.22e-08 ) ( R ) = ( 1.05e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00489288 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582293 s | Solve Time: 0.331665 s + compositionalMultiphaseFlow: Max pressure change: 6706.486 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.155 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5297913763822066e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 4.19e-08 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.134273172226813e-10 + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 4.16e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0773087977256068e-09 + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 4.93e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.717825350501585e-10 + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 5.51e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.191321816866434e-10 + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 5.85e-08 ) ( R ) = ( 1.06e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00552239 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586163 s | Solve Time: 0.332039 s + compositionalMultiphaseFlow: Max pressure change: 6287.646 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.021 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.883733696279478e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ( Rwell ) = ( 3.68e-08 ) ( R ) = ( 1.42e-03 ) + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.228464328155269e-10 + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 3.84e-08 ) ( R ) = ( 1.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1071642491700118e-09 + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 4.62e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.428323594600329e-10 + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 5.18e-08 ) ( R ) = ( 1.11e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.936953068579442e-10 + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 5.50e-08 ) ( R ) = ( 1.08e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00523281 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581708 s | Solve Time: 0.331301 s + compositionalMultiphaseFlow: Max pressure change: 5895.267 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.895 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9836183523812565e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 3.24e-08 ) ( R ) = ( 1.20e-03 ) + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.16978682085778e-10 + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 3.56e-08 ) ( R ) = ( 1.14e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0922338589125502e-09 + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 4.33e-08 ) ( R ) = ( 1.11e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.055108802196287e-10 + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 4.86e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.675761999806127e-10 + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 5.17e-08 ) ( R ) = ( 1.09e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00472732 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583834 s | Solve Time: 0.332105 s + compositionalMultiphaseFlow: Max pressure change: 5527.387 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.772 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0649064397536563e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.14e-04 ) ( Rwell ) = ( 2.85e-08 ) ( R ) = ( 9.14e-04 ) + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000006265 Pa +wellControls1: Total rate: -890.5565453794158 mol/s; total surface volumetric rate: -21.044417069916843 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -21.044417069916843 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.166 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.37679e+06, 8.97492e+06, 9.19325e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.94223e+06, -2.14371e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26507e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.3976e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92531e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26507e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.24241e+12, 2.26575e+10 } } mol +Time: 6.13e+08 s, dt: 4320000 s, Cycle: 155 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.71e-03 ) ( Rwell ) = ( 2.85e-08 ) ( R ) = ( 1.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00444132 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583596 s | Solve Time: 0.332325 s + compositionalMultiphaseFlow: Max pressure change: 15202.781 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.916 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.750695959896632e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-03 ) ( Rwell ) = ( 2.15e-07 ) ( R ) = ( 2.28e-03 ) + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1880407818919423e-08 + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ( Rwell ) = ( 6.79e-08 ) ( R ) = ( 9.16e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00537606 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580497 s | Solve Time: 0.332467 s + compositionalMultiphaseFlow: Max pressure change: 7601.117 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.442 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7217304248973164e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ( Rwell ) = ( 5.38e-08 ) ( R ) = ( 1.65e-03 ) + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3516565644522416e-09 + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 4.74e-08 ) ( R ) = ( 1.24e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.84100800849319e-10 + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 5.43e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.065623807202883e-10 + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ( Rwell ) = ( 6.02e-08 ) ( R ) = ( 9.37e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.568498995245363e-10 + Line search @ 0.062: ( Rflow ) = ( 8.86e-04 ) ( Rwell ) = ( 6.38e-08 ) ( R ) = ( 8.86e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00484861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583077 s | Solve Time: 0.332501 s + compositionalMultiphaseFlow: Max pressure change: 7127.754 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.294 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0471120354415007e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 4.73e-08 ) ( R ) = ( 1.30e-03 ) + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0091627533626024e-09 + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 4.37e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0073865075455046e-09 + Line search @ 0.250: ( Rflow ) = ( 9.90e-04 ) ( Rwell ) = ( 5.08e-08 ) ( R ) = ( 9.90e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.747835789080227e-10 + Line search @ 0.125: ( Rflow ) = ( 9.38e-04 ) ( Rwell ) = ( 5.66e-08 ) ( R ) = ( 9.38e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.301153960246552e-10 + Line search @ 0.062: ( Rflow ) = ( 9.12e-04 ) ( Rwell ) = ( 6.00e-08 ) ( R ) = ( 9.12e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00531595 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587769 s | Solve Time: 0.331575 s + compositionalMultiphaseFlow: Max pressure change: 6681.158 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.147 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4125174080680267e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.42e-03 ) ( Rwell ) = ( 4.15e-08 ) ( R ) = ( 1.42e-03 ) + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.616142161381845e-10 + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 4.04e-08 ) ( R ) = ( 1.17e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0384010318276182e-09 + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 4.76e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.451463973102591e-10 + Line search @ 0.125: ( Rflow ) = ( 9.75e-04 ) ( Rwell ) = ( 5.32e-08 ) ( R ) = ( 9.75e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.04019381786236e-10 + Line search @ 0.062: ( Rflow ) = ( 9.43e-04 ) ( Rwell ) = ( 5.64e-08 ) ( R ) = ( 9.43e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00512504 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.596475 s | Solve Time: 0.331314 s + compositionalMultiphaseFlow: Max pressure change: 6264.252 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.013 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.571074020352171e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 3.65e-08 ) ( R ) = ( 1.24e-03 ) + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.593877666105641e-10 + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 3.74e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0322644961036076e-09 + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 4.46e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.078313573633977e-10 + Line search @ 0.125: ( Rflow ) = ( 9.80e-04 ) ( Rwell ) = ( 5.00e-08 ) ( R ) = ( 9.80e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.768069272742537e-10 + Line search @ 0.062: ( Rflow ) = ( 9.62e-04 ) ( Rwell ) = ( 5.31e-08 ) ( R ) = ( 9.62e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00527417 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588101 s | Solve Time: 0.331652 s + compositionalMultiphaseFlow: Max pressure change: 5873.050 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.888 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.829367740098121e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 3.21e-08 ) ( R ) = ( 1.23e-03 ) + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.163198757429655e-10 + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 3.46e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0505912806380024e-09 + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 4.18e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.823837133713596e-10 + Line search @ 0.125: ( Rflow ) = ( 9.95e-04 ) ( Rwell ) = ( 4.69e-08 ) ( R ) = ( 9.95e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5543624427324403e-10 + Line search @ 0.062: ( Rflow ) = ( 9.78e-04 ) ( Rwell ) = ( 4.99e-08 ) ( R ) = ( 9.78e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00513677 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580553 s | Solve Time: 0.332023 s + compositionalMultiphaseFlow: Max pressure change: 5506.202 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.770 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8851037114918654e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 2.83e-08 ) ( R ) = ( 1.08e-03 ) + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.3734272587036e-10 + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 3.20e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0271858918997623e-09 + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 3.92e-08 ) ( R ) = ( 1.00e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.427348736044337e-10 + Line search @ 0.125: ( Rflow ) = ( 9.91e-04 ) ( Rwell ) = ( 4.41e-08 ) ( R ) = ( 9.91e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.286300203659721e-10 + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ( Rwell ) = ( 4.69e-08 ) ( R ) = ( 9.85e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00526677 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584565 s | Solve Time: 0.331801 s + compositionalMultiphaseFlow: Max pressure change: 5162.310 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.660 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0103659565128282e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 2.48e-08 ) ( R ) = ( 1.08e-03 ) + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.647585732404536e-10 + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 2.96e-08 ) ( R ) = ( 1.03e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0220790880310915e-09 + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 3.67e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.129162815644463e-10 + Line search @ 0.125: ( Rflow ) = ( 9.96e-04 ) ( Rwell ) = ( 4.14e-08 ) ( R ) = ( 9.96e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.0690806279997105e-10 + Line search @ 0.062: ( Rflow ) = ( 9.91e-04 ) ( Rwell ) = ( 4.40e-08 ) ( R ) = ( 9.91e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00463415 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584132 s | Solve Time: 0.331372 s + compositionalMultiphaseFlow: Max pressure change: 4840.145 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.555 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0191215083519296e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.78e-04 ) ( Rwell ) = ( 2.19e-08 ) ( R ) = ( 7.78e-04 ) + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999999832 Pa +wellControls1: Total rate: -887.2723352125545 mol/s; total surface volumetric rate: -20.966809236222804 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.966809236222804 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.36727e+06, 8.96009e+06, 9.17805e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.9518e+06, -2.15839e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26124e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.39185e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92205e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26124e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.23862e+12, 2.26194e+10 } } mol +Time: 6.17e+08 s, dt: 4320000 s, Cycle: 156 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.71e-03 ) ( Rwell ) = ( 2.19e-08 ) ( R ) = ( 1.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00539529 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588206 s | Solve Time: 0.331249 s + compositionalMultiphaseFlow: Max pressure change: 15143.424 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.895 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7535720481530745e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-03 ) ( Rwell ) = ( 2.13e-07 ) ( R ) = ( 3.36e-03 ) + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1624365631467413e-08 + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ( Rwell ) = ( 6.41e-08 ) ( R ) = ( 1.31e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00508106 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583024 s | Solve Time: 0.331448 s + compositionalMultiphaseFlow: Max pressure change: 7573.903 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.425 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1558330959005048e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ( Rwell ) = ( 5.34e-08 ) ( R ) = ( 1.47e-03 ) + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.933532334241761e-09 + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ( Rwell ) = ( 4.54e-08 ) ( R ) = ( 1.39e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.403785362569693e-10 + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 5.14e-08 ) ( R ) = ( 1.35e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.964994219733512e-10 + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 5.69e-08 ) ( R ) = ( 1.33e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.047677831271358e-10 + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ( Rwell ) = ( 6.03e-08 ) ( R ) = ( 1.32e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00519861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585733 s | Solve Time: 0.331872 s + compositionalMultiphaseFlow: Max pressure change: 7100.869 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.274 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3083836236660318e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ( Rwell ) = ( 4.69e-08 ) ( R ) = ( 1.45e-03 ) + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4145701277001876e-09 + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ( Rwell ) = ( 4.19e-08 ) ( R ) = ( 1.38e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.974257920650984e-10 + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 4.82e-08 ) ( R ) = ( 1.35e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.744973551382373e-10 + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 5.35e-08 ) ( R ) = ( 1.33e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.811457898767912e-10 + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 5.67e-08 ) ( R ) = ( 1.33e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00543841 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584496 s | Solve Time: 0.331498 s + compositionalMultiphaseFlow: Max pressure change: 6657.295 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.131 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6202784669516745e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.50e-03 ) ( Rwell ) = ( 4.12e-08 ) ( R ) = ( 1.50e-03 ) + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0252789728326661e-09 + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ( Rwell ) = ( 3.87e-08 ) ( R ) = ( 1.41e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.45382097658387e-10 + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ( Rwell ) = ( 4.51e-08 ) ( R ) = ( 1.37e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.524166845129798e-10 + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 5.03e-08 ) ( R ) = ( 1.35e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5859915864809864e-10 + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ( Rwell ) = ( 5.34e-08 ) ( R ) = ( 1.34e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00490189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584554 s | Solve Time: 0.331976 s + compositionalMultiphaseFlow: Max pressure change: 6242.265 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.001 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.772352598017335e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 3.63e-08 ) ( R ) = ( 1.13e-03 ) + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00977015 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581623 s | Solve Time: 0.253185 s + compositionalMultiphaseFlow: Max pressure change: 5.004 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.046 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.340392988413157e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.88e-06 ) ( Rwell ) = ( 1.10e-10 ) ( R ) = ( 1.88e-06 ) + Last LinSolve(iter,res) = ( 3, 9.77e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000002899 Pa +wellControls1: Total rate: -884.0058213665997 mol/s; total surface volumetric rate: -20.889620243835047 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.889620243835047 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.35777e+06, 8.94532e+06, 9.1629e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.96132e+06, -2.17301e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.25742e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.38613e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9188e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.25742e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.23484e+12, 2.25813e+10 } } mol +Time: 6.21e+08 s, dt: 4320000 s, Cycle: 157 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-03 ) ( Rwell ) = ( 1.10e-10 ) ( R ) = ( 1.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00494708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583724 s | Solve Time: 0.331624 s + compositionalMultiphaseFlow: Max pressure change: 15088.057 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.878 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.062529008168724e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-03 ) ( Rwell ) = ( 2.11e-07 ) ( R ) = ( 2.83e-03 ) + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2974986246815376e-08 + Line search @ 0.500: ( Rflow ) = ( 8.86e-04 ) ( Rwell ) = ( 5.27e-08 ) ( R ) = ( 8.86e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00463401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583831 s | Solve Time: 0.332161 s + compositionalMultiphaseFlow: Max pressure change: 7546.540 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.419 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5096620620269618e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 5.29e-08 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.691493028450509e-09 + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ( Rwell ) = ( 3.96e-08 ) ( R ) = ( 9.40e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2608449274107443e-10 + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ( Rwell ) = ( 4.29e-08 ) ( R ) = ( 8.01e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00546876 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584016 s | Solve Time: 0.331723 s + compositionalMultiphaseFlow: Max pressure change: 5659.222 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.818 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3550226496406026e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 2.98e-08 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.819527247932001e-10 + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 2.89e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.482142600461316e-10 + Line search @ 0.250: ( Rflow ) = ( 9.21e-04 ) ( Rwell ) = ( 3.40e-08 ) ( R ) = ( 9.21e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.558937754557292e-10 + Line search @ 0.125: ( Rflow ) = ( 8.61e-04 ) ( Rwell ) = ( 3.80e-08 ) ( R ) = ( 8.61e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.358689992793984e-10 + Line search @ 0.062: ( Rflow ) = ( 8.31e-04 ) ( Rwell ) = ( 4.03e-08 ) ( R ) = ( 8.31e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00511651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584976 s | Solve Time: 0.331852 s + compositionalMultiphaseFlow: Max pressure change: 5305.601 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.709 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.488241641034449e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 2.62e-08 ) ( R ) = ( 1.04e-03 ) + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.403545471656003e-10 + Line search @ 0.500: ( Rflow ) = ( 9.35e-04 ) ( Rwell ) = ( 2.67e-08 ) ( R ) = ( 9.35e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.492104631661277e-10 + Line search @ 0.250: ( Rflow ) = ( 8.83e-04 ) ( Rwell ) = ( 3.19e-08 ) ( R ) = ( 8.83e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.322112750505426e-10 + Line search @ 0.125: ( Rflow ) = ( 8.57e-04 ) ( Rwell ) = ( 3.57e-08 ) ( R ) = ( 8.57e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.1798708111097085e-10 + Line search @ 0.062: ( Rflow ) = ( 8.44e-04 ) ( Rwell ) = ( 3.79e-08 ) ( R ) = ( 8.44e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00530083 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580783 s | Solve Time: 0.331282 s + compositionalMultiphaseFlow: Max pressure change: 4974.524 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.598 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6668563196375885e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 2.30e-08 ) ( R ) = ( 1.07e-03 ) + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.12981768174825e-10 + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ( Rwell ) = ( 2.47e-08 ) ( R ) = ( 9.55e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.612571601394279e-10 + Line search @ 0.250: ( Rflow ) = ( 8.99e-04 ) ( Rwell ) = ( 2.99e-08 ) ( R ) = ( 8.99e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.138237613167007e-10 + Line search @ 0.125: ( Rflow ) = ( 8.71e-04 ) ( Rwell ) = ( 3.35e-08 ) ( R ) = ( 8.71e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0269398099136424e-10 + Line search @ 0.062: ( Rflow ) = ( 8.57e-04 ) ( Rwell ) = ( 3.56e-08 ) ( R ) = ( 8.57e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00479147 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580895 s | Solve Time: 0.331217 s + compositionalMultiphaseFlow: Max pressure change: 4664.661 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.508 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7415963116107491e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.34e-04 ) ( Rwell ) = ( 2.02e-08 ) ( R ) = ( 8.34e-04 ) + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000001672 Pa +wellControls1: Total rate: -880.7581434267541 mol/s; total surface volumetric rate: -20.812874781792548 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.812874781792548 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.34832e+06, 8.9306e+06, 9.14781e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.97082e+06, -2.18758e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.25361e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.38042e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91557e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.25361e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.23107e+12, 2.25435e+10 } } mol +Time: 6.26e+08 s, dt: 4320000 s, Cycle: 158 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-03 ) ( Rwell ) = ( 2.02e-08 ) ( R ) = ( 1.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00520041 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581861 s | Solve Time: 0.331907 s + compositionalMultiphaseFlow: Max pressure change: 15031.500 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.859 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7739499808276946e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.11e-03 ) ( Rwell ) = ( 2.10e-07 ) ( R ) = ( 3.11e-03 ) + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.170255453126657e-08 + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 6.26e-08 ) ( R ) = ( 1.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00528865 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583539 s | Solve Time: 0.331558 s + compositionalMultiphaseFlow: Max pressure change: 7517.474 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.407 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.162663965104116e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ( Rwell ) = ( 5.26e-08 ) ( R ) = ( 1.62e-03 ) + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9055845790205694e-09 + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ( Rwell ) = ( 4.44e-08 ) ( R ) = ( 1.41e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.157320291995006e-10 + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ( Rwell ) = ( 5.02e-08 ) ( R ) = ( 1.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.745324381858154e-10 + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 5.56e-08 ) ( R ) = ( 1.26e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.913746076695702e-10 + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 5.89e-08 ) ( R ) = ( 1.24e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00536219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588533 s | Solve Time: 0.331711 s + compositionalMultiphaseFlow: Max pressure change: 7047.727 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.256 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2577163754912135e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ( Rwell ) = ( 4.62e-08 ) ( R ) = ( 1.55e-03 ) + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.40527012248981e-09 + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ( Rwell ) = ( 4.10e-08 ) ( R ) = ( 1.39e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.70187136289735e-10 + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ( Rwell ) = ( 4.70e-08 ) ( R ) = ( 1.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.529153966956414e-10 + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 5.22e-08 ) ( R ) = ( 1.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.683650134396089e-10 + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 5.54e-08 ) ( R ) = ( 1.26e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00528279 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581733 s | Solve Time: 0.33188 s + compositionalMultiphaseFlow: Max pressure change: 6607.499 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.116 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4735777043028975e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.41e-03 ) ( Rwell ) = ( 4.06e-08 ) ( R ) = ( 1.41e-03 ) + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.069511146312152e-09 + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 3.78e-08 ) ( R ) = ( 1.33e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.045896171537947e-10 + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 4.41e-08 ) ( R ) = ( 1.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.28940574568071e-10 + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 4.91e-08 ) ( R ) = ( 1.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.460923852533938e-10 + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 5.21e-08 ) ( R ) = ( 1.26e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00468313 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584764 s | Solve Time: 0.331483 s + compositionalMultiphaseFlow: Max pressure change: 6195.614 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.987 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.643946312412936e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ( Rwell ) = ( 3.58e-08 ) ( R ) = ( 1.03e-03 ) + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00899274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585643 s | Solve Time: 0.252741 s + compositionalMultiphaseFlow: Max pressure change: 4.068 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.045 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.307387612203286e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-06 ) ( Rwell ) = ( 1.33e-10 ) ( R ) = ( 1.33e-06 ) + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999984356 Pa +wellControls1: Total rate: -877.5273539445872 mol/s; total surface volumetric rate: -20.736529896342407 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.736529896342407 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.33889e+06, 8.91593e+06, 9.13278e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.98027e+06, -2.2021e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24982e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.37473e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91235e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24982e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.22732e+12, 2.25057e+10 } } mol +Time: 6.30e+08 s, dt: 1320000 s, Cycle: 159 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-04 ) ( Rwell ) = ( 1.33e-10 ) ( R ) = ( 5.16e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00600661 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582934 s | Solve Time: 0.252483 s + compositionalMultiphaseFlow: Max pressure change: 4589.850 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.508 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0295075337249955e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 1.96e-08 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 3, 6.01e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999997637 Pa +wellControls1: Total rate: -876.5420300468716 mol/s; total surface volumetric rate: -20.71324564863741 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.71324564863741 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.050 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.33601e+06, 8.91146e+06, 9.12819e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.9897e+06, -2.21656e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24866e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.373e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91136e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24866e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.22617e+12, 2.24942e+10 } } mol +Time: 6.31e+08 s, dt: 2640000 s, Cycle: 160 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 1.96e-08 ) ( R ) = ( 1.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00859347 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585441 s | Solve Time: 0.252081 s + compositionalMultiphaseFlow: Max pressure change: 9158.457 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.063 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.288667612850077e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.16e-04 ) ( Rwell ) = ( 7.79e-08 ) ( R ) = ( 7.16e-04 ) + Last LinSolve(iter,res) = ( 3, 8.59e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999997697 Pa +wellControls1: Total rate: -874.578004822284 mol/s; total surface volumetric rate: -20.666833932678284 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.666833932678284 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.100 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.33027e+06, 8.90252e+06, 9.11903e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.99258e+06, -2.22097e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24636e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.36953e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9094e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24636e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.22388e+12, 2.24713e+10 } } mol +Time: 6.34e+08 s, dt: 4320000 s, Cycle: 161 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-03 ) ( Rwell ) = ( 7.79e-08 ) ( R ) = ( 2.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00543725 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583339 s | Solve Time: 0.331554 s + compositionalMultiphaseFlow: Max pressure change: 14929.423 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.826 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0102271180988396e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-03 ) ( Rwell ) = ( 2.07e-07 ) ( R ) = ( 3.37e-03 ) + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7643547844947705e-08 + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ( Rwell ) = ( 9.06e-08 ) ( R ) = ( 9.77e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00585162 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584886 s | Solve Time: 0.331654 s + compositionalMultiphaseFlow: Max pressure change: 7468.324 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.398 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.228637078857901e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-03 ) ( Rwell ) = ( 5.18e-08 ) ( R ) = ( 2.08e-03 ) + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.571291430302324e-09 + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 5.83e-08 ) ( R ) = ( 1.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8604897622509498e-09 + Line search @ 0.250: ( Rflow ) = ( 7.72e-04 ) ( Rwell ) = ( 7.12e-08 ) ( R ) = ( 7.72e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00501661 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582305 s | Solve Time: 0.332408 s + compositionalMultiphaseFlow: Max pressure change: 5602.442 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.798 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.69537816907939e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 2.95e-08 ) ( R ) = ( 1.09e-03 ) + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6931624990945693e-09 + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ( Rwell ) = ( 4.29e-08 ) ( R ) = ( 9.32e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7645532812693432e-09 + Line search @ 0.250: ( Rflow ) = ( 8.52e-04 ) ( Rwell ) = ( 5.52e-08 ) ( R ) = ( 8.52e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.137485217128642e-09 + Line search @ 0.125: ( Rflow ) = ( 8.12e-04 ) ( Rwell ) = ( 6.28e-08 ) ( R ) = ( 8.12e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.325197032808205e-10 + Line search @ 0.062: ( Rflow ) = ( 7.92e-04 ) ( Rwell ) = ( 6.69e-08 ) ( R ) = ( 7.92e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00541704 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582672 s | Solve Time: 0.33121 s + compositionalMultiphaseFlow: Max pressure change: 5252.400 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.683 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.694096083530553e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ( Rwell ) = ( 2.59e-08 ) ( R ) = ( 1.18e-03 ) + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6578821648849384e-09 + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ( Rwell ) = ( 3.99e-08 ) ( R ) = ( 9.86e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.721007780730588e-09 + Line search @ 0.250: ( Rflow ) = ( 8.89e-04 ) ( Rwell ) = ( 5.18e-08 ) ( R ) = ( 8.89e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.083352074715549e-09 + Line search @ 0.125: ( Rflow ) = ( 8.40e-04 ) ( Rwell ) = ( 5.89e-08 ) ( R ) = ( 8.40e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.973674888082314e-10 + Line search @ 0.062: ( Rflow ) = ( 8.16e-04 ) ( Rwell ) = ( 6.28e-08 ) ( R ) = ( 8.16e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00588695 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585175 s | Solve Time: 0.331085 s + compositionalMultiphaseFlow: Max pressure change: 4924.555 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.584 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.6984447160957075e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ( Rwell ) = ( 2.27e-08 ) ( R ) = ( 1.39e-03 ) + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8210555285946839e-09 + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 3.70e-08 ) ( R ) = ( 1.10e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6818096915116598e-09 + Line search @ 0.250: ( Rflow ) = ( 9.59e-04 ) ( Rwell ) = ( 4.85e-08 ) ( R ) = ( 9.59e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0335881039935657e-09 + Line search @ 0.125: ( Rflow ) = ( 8.87e-04 ) ( Rwell ) = ( 5.53e-08 ) ( R ) = ( 8.87e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.649475331992448e-10 + Line search @ 0.062: ( Rflow ) = ( 8.52e-04 ) ( Rwell ) = ( 5.90e-08 ) ( R ) = ( 8.52e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00546788 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581957 s | Solve Time: 0.331118 s + compositionalMultiphaseFlow: Max pressure change: 4616.807 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.481 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.487783893975973e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 2.01e-08 ) ( R ) = ( 1.05e-03 ) + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.808446725704016e-09 + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ( Rwell ) = ( 3.44e-08 ) ( R ) = ( 9.51e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6059393814771283e-09 + Line search @ 0.250: ( Rflow ) = ( 9.01e-04 ) ( Rwell ) = ( 4.55e-08 ) ( R ) = ( 9.01e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.782828991333758e-10 + Line search @ 0.125: ( Rflow ) = ( 8.77e-04 ) ( Rwell ) = ( 5.19e-08 ) ( R ) = ( 8.77e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.329554575439488e-10 + Line search @ 0.062: ( Rflow ) = ( 8.64e-04 ) ( Rwell ) = ( 5.54e-08 ) ( R ) = ( 8.64e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00510109 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58659 s | Solve Time: 0.331268 s + compositionalMultiphaseFlow: Max pressure change: 4328.547 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.392 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.261407420853459e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.74e-04 ) ( Rwell ) = ( 1.77e-08 ) ( R ) = ( 8.74e-04 ) + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999413 Pa +wellControls1: Total rate: -871.3824377728333 mol/s; total surface volumetric rate: -20.591321158844373 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.591321158844373 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.32092e+06, 8.88796e+06, 9.10411e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -4.99832e+06, -2.22978e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24259e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.36389e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9062e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24259e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.22016e+12, 2.24339e+10 } } mol +Time: 6.38e+08 s, dt: 4320000 s, Cycle: 162 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-03 ) ( Rwell ) = ( 1.77e-08 ) ( R ) = ( 1.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00505986 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583324 s | Solve Time: 0.331602 s + compositionalMultiphaseFlow: Max pressure change: 14870.553 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.808 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8191516898701252e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-03 ) ( Rwell ) = ( 2.05e-07 ) ( R ) = ( 2.97e-03 ) + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.200043858202605e-08 + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ( Rwell ) = ( 6.01e-08 ) ( R ) = ( 1.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00530682 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58291 s | Solve Time: 0.33187 s + compositionalMultiphaseFlow: Max pressure change: 7437.597 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.382 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0788377968751206e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ( Rwell ) = ( 5.15e-08 ) ( R ) = ( 1.64e-03 ) + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8396674184018025e-09 + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ( Rwell ) = ( 4.29e-08 ) ( R ) = ( 1.40e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.356275588676908e-10 + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 4.83e-08 ) ( R ) = ( 1.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.812234192883238e-10 + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 5.34e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.939072484333451e-10 + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 5.65e-08 ) ( R ) = ( 1.20e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0049178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58227 s | Solve Time: 0.331359 s + compositionalMultiphaseFlow: Max pressure change: 6973.004 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.239 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.199839450016782e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ( Rwell ) = ( 4.53e-08 ) ( R ) = ( 1.33e-03 ) + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.438277275056521e-09 + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 3.96e-08 ) ( R ) = ( 1.27e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.661762335686717e-10 + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 4.52e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.540364999059079e-10 + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 5.02e-08 ) ( R ) = ( 1.22e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.697074951209856e-10 + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 5.32e-08 ) ( R ) = ( 1.21e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00534412 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584469 s | Solve Time: 0.331536 s + compositionalMultiphaseFlow: Max pressure change: 6538.829 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.107 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6474978048464095e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-03 ) ( Rwell ) = ( 3.97e-08 ) ( R ) = ( 1.57e-03 ) + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.806045892484349e-10 + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ( Rwell ) = ( 3.65e-08 ) ( R ) = ( 1.39e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.383160832181602e-10 + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ( Rwell ) = ( 4.23e-08 ) ( R ) = ( 1.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.385034805906798e-10 + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 4.71e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.490497973463903e-10 + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 5.00e-08 ) ( R ) = ( 1.23e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0053525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582992 s | Solve Time: 0.331282 s + compositionalMultiphaseFlow: Max pressure change: 6130.329 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.976 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9544099671975346e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.48e-03 ) ( Rwell ) = ( 3.49e-08 ) ( R ) = ( 1.48e-03 ) + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.330050927871866e-10 + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ( Rwell ) = ( 3.37e-08 ) ( R ) = ( 1.36e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.668560314006868e-10 + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 3.97e-08 ) ( R ) = ( 1.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.167147986208988e-10 + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 4.43e-08 ) ( R ) = ( 1.26e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.291473842954474e-10 + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 4.70e-08 ) ( R ) = ( 1.25e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00532274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581381 s | Solve Time: 0.331532 s + compositionalMultiphaseFlow: Max pressure change: 5746.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.843 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.050311587176168e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ( Rwell ) = ( 3.07e-08 ) ( R ) = ( 1.26e-03 ) + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.353781862282858e-10 + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 3.12e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.530596229405774e-10 + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 3.72e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.815537023641127e-10 + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 4.16e-08 ) ( R ) = ( 1.25e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.045060952861945e-10 + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 4.42e-08 ) ( R ) = ( 1.25e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00496604 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583593 s | Solve Time: 0.331479 s + compositionalMultiphaseFlow: Max pressure change: 5388.219 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.738 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.217695915796014e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 2.71e-08 ) ( R ) = ( 1.07e-03 ) + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00157104 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584389 s | Solve Time: 0.331279 s + compositionalMultiphaseFlow: Max pressure change: 4.272 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.044 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.821019250478287e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.23e-07 ) ( Rwell ) = ( 9.89e-11 ) ( R ) = ( 7.23e-07 ) + Last LinSolve(iter,res) = ( 4, 1.57e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999146 Pa +wellControls1: Total rate: -868.2027639978429 mol/s; total surface volumetric rate: -20.516184339557196 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.516184339557196 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.3116e+06, 8.87345e+06, 9.08924e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.00767e+06, -2.24415e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23884e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.35826e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90301e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23884e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.21644e+12, 2.23965e+10 } } mol +Time: 6.42e+08 s, dt: 4320000 s, Cycle: 163 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-03 ) ( Rwell ) = ( 9.91e-11 ) ( R ) = ( 1.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00444743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585551 s | Solve Time: 0.331708 s + compositionalMultiphaseFlow: Max pressure change: 14819.391 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.790 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.044832275200804e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ( Rwell ) = ( 2.04e-07 ) ( R ) = ( 2.29e-03 ) + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.284896860604846e-08 + Line search @ 0.500: ( Rflow ) = ( 8.75e-04 ) ( Rwell ) = ( 5.10e-08 ) ( R ) = ( 8.75e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00520637 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585808 s | Solve Time: 0.331656 s + compositionalMultiphaseFlow: Max pressure change: 7408.685 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.380 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2021775797066425e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ( Rwell ) = ( 5.10e-08 ) ( R ) = ( 1.60e-03 ) + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4073875115604437e-09 + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ( Rwell ) = ( 3.82e-08 ) ( R ) = ( 1.00e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.6699743244383853e-10 + Line search @ 0.250: ( Rflow ) = ( 7.00e-04 ) ( Rwell ) = ( 4.14e-08 ) ( R ) = ( 7.00e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0053337 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582882 s | Solve Time: 0.33317 s + compositionalMultiphaseFlow: Max pressure change: 5557.449 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.787 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3647388774629121e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 2.87e-08 ) ( R ) = ( 1.23e-03 ) + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.989358064008911e-10 + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ( Rwell ) = ( 2.79e-08 ) ( R ) = ( 9.63e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.396280172182855e-10 + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ( Rwell ) = ( 3.29e-08 ) ( R ) = ( 8.32e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.484458442950313e-10 + Line search @ 0.125: ( Rflow ) = ( 7.66e-04 ) ( Rwell ) = ( 3.67e-08 ) ( R ) = ( 7.66e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.313574969965316e-10 + Line search @ 0.062: ( Rflow ) = ( 7.33e-04 ) ( Rwell ) = ( 3.89e-08 ) ( R ) = ( 7.33e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00455594 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585317 s | Solve Time: 0.331585 s + compositionalMultiphaseFlow: Max pressure change: 5210.945 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.672 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4350773902549463e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.39e-04 ) ( Rwell ) = ( 2.53e-08 ) ( R ) = ( 8.39e-04 ) + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.9999999101 Pa +wellControls1: Total rate: -865.0413073487175 mol/s; total surface volumetric rate: -20.441476276462748 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.441476276462748 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.163 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.30231e+06, 8.85899e+06, 9.07442e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.01699e+06, -2.25846e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.2351e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.35266e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89984e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.2351e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.21274e+12, 2.23594e+10 } } mol +Time: 6.47e+08 s, dt: 4320000 s, Cycle: 164 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-03 ) ( Rwell ) = ( 2.53e-08 ) ( R ) = ( 1.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00458672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582563 s | Solve Time: 0.335124 s + compositionalMultiphaseFlow: Max pressure change: 14766.401 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.782 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6892755911056554e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-03 ) ( Rwell ) = ( 2.02e-07 ) ( R ) = ( 2.51e-03 ) + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.128064902073845e-08 + Line search @ 0.500: ( Rflow ) = ( 9.19e-04 ) ( Rwell ) = ( 6.32e-08 ) ( R ) = ( 9.19e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00458521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583996 s | Solve Time: 0.331916 s + compositionalMultiphaseFlow: Max pressure change: 7382.292 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.374 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2774268309811987e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 5.07e-08 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5818508725118363e-09 + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ( Rwell ) = ( 4.43e-08 ) ( R ) = ( 1.07e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.621590108504051e-10 + Line search @ 0.250: ( Rflow ) = ( 9.93e-04 ) ( Rwell ) = ( 5.06e-08 ) ( R ) = ( 9.93e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.439001719651174e-10 + Line search @ 0.125: ( Rflow ) = ( 9.56e-04 ) ( Rwell ) = ( 5.61e-08 ) ( R ) = ( 9.56e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.250988532878864e-10 + Line search @ 0.062: ( Rflow ) = ( 9.37e-04 ) ( Rwell ) = ( 5.95e-08 ) ( R ) = ( 9.37e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00463726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585888 s | Solve Time: 0.331253 s + compositionalMultiphaseFlow: Max pressure change: 6920.262 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.227 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6321400897467697e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 4.46e-08 ) ( R ) = ( 1.16e-03 ) + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1722343096209897e-09 + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ( Rwell ) = ( 4.09e-08 ) ( R ) = ( 1.05e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.964884390394445e-10 + Line search @ 0.250: ( Rflow ) = ( 9.91e-04 ) ( Rwell ) = ( 4.74e-08 ) ( R ) = ( 9.91e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.139976470644683e-10 + Line search @ 0.125: ( Rflow ) = ( 9.64e-04 ) ( Rwell ) = ( 5.27e-08 ) ( R ) = ( 9.64e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.983904400290839e-10 + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ( Rwell ) = ( 5.59e-08 ) ( R ) = ( 9.51e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00495114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584437 s | Solve Time: 0.331432 s + compositionalMultiphaseFlow: Max pressure change: 6488.320 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.085 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.036728008469879e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 3.92e-08 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.995557632118789e-10 + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 3.78e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.386649235665345e-10 + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 4.44e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.909616295265209e-10 + Line search @ 0.125: ( Rflow ) = ( 9.84e-04 ) ( Rwell ) = ( 4.95e-08 ) ( R ) = ( 9.84e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.758491378709095e-10 + Line search @ 0.062: ( Rflow ) = ( 9.67e-04 ) ( Rwell ) = ( 5.26e-08 ) ( R ) = ( 9.67e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00516163 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583719 s | Solve Time: 0.332106 s + compositionalMultiphaseFlow: Max pressure change: 6083.389 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.963 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2942572286410723e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.27e-03 ) ( Rwell ) = ( 3.45e-08 ) ( R ) = ( 1.27e-03 ) + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.430043164584731e-10 + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ( Rwell ) = ( 3.49e-08 ) ( R ) = ( 1.12e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.518498211846804e-10 + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 4.16e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.592396711331162e-10 + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 4.65e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5041703700121616e-10 + Line search @ 0.062: ( Rflow ) = ( 9.86e-04 ) ( Rwell ) = ( 4.94e-08 ) ( R ) = ( 9.86e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0048902 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587116 s | Solve Time: 0.330549 s + compositionalMultiphaseFlow: Max pressure change: 5703.067 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.835 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4480205640387e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 3.03e-08 ) ( R ) = ( 1.09e-03 ) + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.892548588486534e-10 + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ( Rwell ) = ( 3.23e-08 ) ( R ) = ( 1.04e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.495334518661025e-10 + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 3.90e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.275809954521151e-10 + Line search @ 0.125: ( Rflow ) = ( 9.99e-04 ) ( Rwell ) = ( 4.37e-08 ) ( R ) = ( 9.99e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.269674613865959e-10 + Line search @ 0.062: ( Rflow ) = ( 9.92e-04 ) ( Rwell ) = ( 4.65e-08 ) ( R ) = ( 9.92e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00483781 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583523 s | Solve Time: 0.33086 s + compositionalMultiphaseFlow: Max pressure change: 5346.869 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.720 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6165891675589137e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.95e-04 ) ( Rwell ) = ( 2.66e-08 ) ( R ) = ( 9.95e-04 ) + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999923 Pa +wellControls1: Total rate: -861.8967182892882 mol/s; total surface volumetric rate: -20.36716747568541 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.36716747568541 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.163 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.29305e+06, 8.84459e+06, 9.05965e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.02628e+06, -2.27272e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23138e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.34707e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89667e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23138e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.20906e+12, 2.23223e+10 } } mol +Time: 6.51e+08 s, dt: 4320000 s, Cycle: 165 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-03 ) ( Rwell ) = ( 2.66e-08 ) ( R ) = ( 1.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00483856 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581822 s | Solve Time: 0.330335 s + compositionalMultiphaseFlow: Max pressure change: 14710.501 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.766 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6801335928361425e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-03 ) ( Rwell ) = ( 2.01e-07 ) ( R ) = ( 2.67e-03 ) + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1302328789829517e-08 + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 6.35e-08 ) ( R ) = ( 1.08e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00494811 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579114 s | Solve Time: 0.331173 s + compositionalMultiphaseFlow: Max pressure change: 7356.797 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.355 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4898443589927979e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ( Rwell ) = ( 5.04e-08 ) ( R ) = ( 1.38e-03 ) + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4485787014351104e-09 + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ( Rwell ) = ( 4.44e-08 ) ( R ) = ( 1.23e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.213475538061289e-10 + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 5.08e-08 ) ( R ) = ( 1.16e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.716356525440005e-10 + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ( Rwell ) = ( 5.64e-08 ) ( R ) = ( 1.12e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.38502353819581e-10 + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ( Rwell ) = ( 5.98e-08 ) ( R ) = ( 1.10e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0048187 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580389 s | Solve Time: 0.330794 s + compositionalMultiphaseFlow: Max pressure change: 6897.164 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.208 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.865890220109634e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ( Rwell ) = ( 4.43e-08 ) ( R ) = ( 1.28e-03 ) + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0205608580449166e-09 + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 4.09e-08 ) ( R ) = ( 1.19e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.541203382923413e-10 + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 4.76e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.422132991015019e-10 + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 5.30e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.123484969615788e-10 + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ( Rwell ) = ( 5.62e-08 ) ( R ) = ( 1.11e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0048904 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584782 s | Solve Time: 0.332203 s + compositionalMultiphaseFlow: Max pressure change: 6466.439 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.071 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2128678889288267e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ( Rwell ) = ( 3.89e-08 ) ( R ) = ( 1.24e-03 ) + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.632736664930917e-10 + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ( Rwell ) = ( 3.78e-08 ) ( R ) = ( 1.18e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.842006098992329e-10 + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 4.46e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.14855960484806e-10 + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ( Rwell ) = ( 4.98e-08 ) ( R ) = ( 1.13e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.88078577554063e-10 + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ( Rwell ) = ( 5.28e-08 ) ( R ) = ( 1.12e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00530208 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584343 s | Solve Time: 0.331109 s + compositionalMultiphaseFlow: Max pressure change: 6063.887 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.948 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6225949190106235e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.46e-03 ) ( Rwell ) = ( 3.42e-08 ) ( R ) = ( 1.46e-03 ) + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.044246214642612e-10 + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ( Rwell ) = ( 3.50e-08 ) ( R ) = ( 1.29e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0267318106826906e-09 + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ( Rwell ) = ( 4.18e-08 ) ( R ) = ( 1.21e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.91285703627409e-10 + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 4.68e-08 ) ( R ) = ( 1.16e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.650921869853164e-10 + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ( Rwell ) = ( 4.97e-08 ) ( R ) = ( 1.14e-03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00462586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579891 s | Solve Time: 0.331121 s + compositionalMultiphaseFlow: Max pressure change: 5684.408 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.823 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5920020574332625e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.52e-04 ) ( Rwell ) = ( 3.01e-08 ) ( R ) = ( 9.52e-04 ) + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999448 Pa +wellControls1: Total rate: -858.7689388577768 mol/s; total surface volumetric rate: -20.29325600976817 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.29325600976817 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.163 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.28383e+06, 8.83023e+06, 9.04494e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.03554e+06, -2.28693e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22767e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.34151e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89352e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22767e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.20539e+12, 2.22855e+10 } } mol +Time: 6.55e+08 s, dt: 4320000 s, Cycle: 166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-03 ) ( Rwell ) = ( 3.01e-08 ) ( R ) = ( 1.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00450628 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582627 s | Solve Time: 0.3313 s + compositionalMultiphaseFlow: Max pressure change: 14657.681 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.737 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6388562779366964e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-03 ) ( Rwell ) = ( 1.99e-07 ) ( R ) = ( 2.34e-03 ) + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1156046137171813e-08 + Line search @ 0.500: ( Rflow ) = ( 9.00e-04 ) ( Rwell ) = ( 6.49e-08 ) ( R ) = ( 9.00e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00485924 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581611 s | Solve Time: 0.331998 s + compositionalMultiphaseFlow: Max pressure change: 7328.784 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.354 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.943233574053238e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ( Rwell ) = ( 5.00e-08 ) ( R ) = ( 1.40e-03 ) + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2135525917500445e-09 + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 4.49e-08 ) ( R ) = ( 1.15e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0326079991074266e-09 + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 5.18e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.257061783785048e-10 + Line search @ 0.125: ( Rflow ) = ( 9.63e-04 ) ( Rwell ) = ( 5.76e-08 ) ( R ) = ( 9.63e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.65148483566702e-10 + Line search @ 0.062: ( Rflow ) = ( 9.31e-04 ) ( Rwell ) = ( 6.10e-08 ) ( R ) = ( 9.31e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00471406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58235 s | Solve Time: 0.331051 s + compositionalMultiphaseFlow: Max pressure change: 6872.245 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.211 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3457503717239092e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-03 ) ( Rwell ) = ( 4.39e-08 ) ( R ) = ( 1.25e-03 ) + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.444890342573785e-10 + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 4.15e-08 ) ( R ) = ( 1.09e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0691391105766002e-09 + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 4.85e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.960184816331207e-10 + Line search @ 0.125: ( Rflow ) = ( 9.71e-04 ) ( Rwell ) = ( 5.41e-08 ) ( R ) = ( 9.71e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.38326161425573e-10 + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ( Rwell ) = ( 5.74e-08 ) ( R ) = ( 9.51e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00463817 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581525 s | Solve Time: 0.331274 s + compositionalMultiphaseFlow: Max pressure change: 6442.514 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.063 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.557125511337688e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-03 ) ( Rwell ) = ( 3.86e-08 ) ( R ) = ( 1.09e-03 ) + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.638258831515031e-10 + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 3.84e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.070521005175351e-09 + Line search @ 0.250: ( Rflow ) = ( 9.85e-04 ) ( Rwell ) = ( 4.55e-08 ) ( R ) = ( 9.85e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.582100585741159e-10 + Line search @ 0.125: ( Rflow ) = ( 9.68e-04 ) ( Rwell ) = ( 5.08e-08 ) ( R ) = ( 9.68e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.098041988560453e-10 + Line search @ 0.062: ( Rflow ) = ( 9.60e-04 ) ( Rwell ) = ( 5.40e-08 ) ( R ) = ( 9.60e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00537205 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582609 s | Solve Time: 0.331322 s + compositionalMultiphaseFlow: Max pressure change: 6039.367 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.942 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9782299959535408e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-03 ) ( Rwell ) = ( 3.39e-08 ) ( R ) = ( 1.44e-03 ) + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.178174555808823e-10 + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ( Rwell ) = ( 3.55e-08 ) ( R ) = ( 1.20e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1142353706361519e-09 + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ( Rwell ) = ( 4.26e-08 ) ( R ) = ( 1.08e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.339874346674492e-10 + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 4.78e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.861799851596516e-10 + Line search @ 0.062: ( Rflow ) = ( 9.90e-04 ) ( Rwell ) = ( 5.07e-08 ) ( R ) = ( 9.90e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00477931 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580071 s | Solve Time: 0.331332 s + compositionalMultiphaseFlow: Max pressure change: 5663.205 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.823 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.995044656728396e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.06e-03 ) ( Rwell ) = ( 2.98e-08 ) ( R ) = ( 1.06e-03 ) + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.348127496418442e-10 + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ( Rwell ) = ( 3.28e-08 ) ( R ) = ( 1.02e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0838012709513123e-09 + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ( Rwell ) = ( 3.99e-08 ) ( R ) = ( 1.01e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.928536716050871e-10 + Line search @ 0.125: ( Rflow ) = ( 9.98e-04 ) ( Rwell ) = ( 4.49e-08 ) ( R ) = ( 9.98e-04 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.591391711272763e-10 + Line search @ 0.062: ( Rflow ) = ( 9.94e-04 ) ( Rwell ) = ( 4.77e-08 ) ( R ) = ( 9.94e-04 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00483422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582866 s | Solve Time: 0.331611 s + compositionalMultiphaseFlow: Max pressure change: 5308.524 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.706 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0785116678089253e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.96e-04 ) ( Rwell ) = ( 2.63e-08 ) ( R ) = ( 9.96e-04 ) + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.000001011 Pa +wellControls1: Total rate: -855.6581267853848 mol/s; total surface volumetric rate: -20.219745595488554 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.219745595488554 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.162 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +compflowStatistics, Region1: Pressure (min, average, max): 6.27465e+06, 8.81593e+06, 9.03028e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.04476e+06, -2.30109e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22397e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.33596e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89038e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22397e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.20173e+12, 2.22487e+10 } } mol +Time: 6.60e+08 s, dt: 3000000 s, Cycle: 167 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-03 ) ( Rwell ) = ( 2.63e-08 ) ( R ) = ( 1.16e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00878835 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58472 s | Solve Time: 0.251743 s + compositionalMultiphaseFlow: Max pressure change: 10156.220 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.401 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1165566915494196e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-03 ) ( Rwell ) = ( 9.59e-08 ) ( R ) = ( 1.35e-03 ) + Last LinSolve(iter,res) = ( 3, 8.79e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.56972301402459e-09 + Line search @ 0.500: ( Rflow ) = ( 8.45e-04 ) ( Rwell ) = ( 3.71e-08 ) ( R ) = ( 8.45e-04 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00337866 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584477 s | Solve Time: 0.331367 s + compositionalMultiphaseFlow: Max pressure change: 5082.357 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1.662 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0407972806401062e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.39e-04 ) ( Rwell ) = ( 2.40e-08 ) ( R ) = ( 9.39e-04 ) + Last LinSolve(iter,res) = ( 4, 3.38e-03 ) +wellControls1: BHP (at the specified reference elevation): 1999999.999999736 Pa +wellControls1: Total rate: -853.5064531458997 mol/s; total surface volumetric rate: -20.168900305247536 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.168900305247536 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.113 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.26828e+06, 8.80603e+06, 9.02013e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.05394e+06, -2.3152e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22141e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.33212e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.8882e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22141e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19919e+12, 2.22232e+10 } } mol +Time: 6.63e+08 s, dt: 4320000 s, Cycle: 168 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.67e-03 ) ( Rwell ) = ( 2.40e-08 ) ( R ) = ( 1.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00495146 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589222 s | Solve Time: 0.334021 s + compositionalMultiphaseFlow: Max pressure change: 14567.009 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.712 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6920396467566832e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-03 ) ( Rwell ) = ( 1.97e-07 ) ( R ) = ( 2.82e-03 ) + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.126347209419066e-08 + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ( Rwell ) = ( 6.12e-08 ) ( R ) = ( 1.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00451832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58309 s | Solve Time: 0.333377 s + compositionalMultiphaseFlow: Max pressure change: 7285.121 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.337 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.682069705744027e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-03 ) ( Rwell ) = ( 4.94e-08 ) ( R ) = ( 1.19e-03 ) + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00954295 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58541 s | Solve Time: 0.253514 s + compositionalMultiphaseFlow: Max pressure change: 4.801 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 0.052 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.849056709614445e-09 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-06 ) ( Rwell ) = ( 2.01e-10 ) ( R ) = ( 2.04e-06 ) + Last LinSolve(iter,res) = ( 3, 9.54e-03 ) +wellControls1: BHP (at the specified reference elevation): 2000000.0000015884 Pa +wellControls1: Total rate: -850.4235122850766 mol/s; total surface volumetric rate: -20.09604926824273 sm3/s +wellControls1: Phase 0 surface volumetric rate: 0 sm3/s +wellControls1: Phase 1 surface volumetric rate: -20.09604926824273 sm3/s +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.162 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 6.25915e+06, 8.79181e+06, 9.00556e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -5.06031e+06, -2.32497e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.21774e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.32661e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.88508e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.21774e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.21866e+10 } } mol +Time: 6.67e+08 s, dt: 4320000 s, Cycle: 169 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e+03 ) ( Rwell ) = ( 4.49e+02 ) ( R ) = ( 4.53e+03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00121326 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584421 s | Solve Time: 0.0962878 s + compositionalMultiphaseFlow: Max pressure change: 3730974.940 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 312663.605 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.4478990335289319 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e+03 ) ( Rwell ) = ( 4.45e+02 ) ( R ) = ( 4.49e+03 ) + Last LinSolve(iter,res) = ( 1, 1.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00101257 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583272 s | Solve Time: 0.096188 s + compositionalMultiphaseFlow: Max pressure change: 2861612.452 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 296845.669 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3516720603096073 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.42e+03 ) ( Rwell ) = ( 4.40e+02 ) ( R ) = ( 4.44e+03 ) + Last LinSolve(iter,res) = ( 1, 1.01e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00462096 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582955 s | Solve Time: 0.25379 s + compositionalMultiphaseFlow: Max pressure change: 4116763.577 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 740263.491 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3438248606283536 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.37e+03 ) ( Rwell ) = ( 4.36e+02 ) ( R ) = ( 4.39e+03 ) + Last LinSolve(iter,res) = ( 3, 4.62e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00134303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588577 s | Solve Time: 0.0960503 s + compositionalMultiphaseFlow: Max pressure change: 3638767.274 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 306394.974 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.02205847677375656 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9162134155201924 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.27e+03 ) ( Rwell ) = ( 4.26e+02 ) ( R ) = ( 4.29e+03 ) + Last LinSolve(iter,res) = ( 1, 1.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00201259 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584628 s | Solve Time: 0.414248 s + compositionalMultiphaseFlow: Max pressure change: 3895076.628 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 317127.418 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.031879990639923826 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.180426854422553 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.13e+03 ) ( Rwell ) = ( 4.13e+02 ) ( R ) = ( 4.15e+03 ) + Last LinSolve(iter,res) = ( 5, 2.01e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.0089872 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583977 s | Solve Time: 1.08174 s + compositionalMultiphaseFlow: Max pressure change: 3135562.270 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 293094.569 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1562114177397156 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.09e+03 ) ( Rwell ) = ( 4.08e+02 ) ( R ) = ( 4.11e+03 ) + Last LinSolve(iter,res) = ( 13, 8.99e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00643475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587762 s | Solve Time: 0.745562 s + compositionalMultiphaseFlow: Max pressure change: 3094242.752 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 374671.075 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1392555697529652 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.04e+03 ) ( Rwell ) = ( 4.04e+02 ) ( R ) = ( 4.06e+03 ) + Last LinSolve(iter,res) = ( 9, 6.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00468008 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5866 s | Solve Time: 0.660665 s + compositionalMultiphaseFlow: Max pressure change: 1772800.327 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 199539.111 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.07615903776855303 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.358008776922922 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.74e+03 ) ( Rwell ) = ( 3.74e+02 ) ( R ) = ( 3.76e+03 ) + Last LinSolve(iter,res) = ( 8, 4.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00429206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584941 s | Solve Time: 0.82598 s + compositionalMultiphaseFlow: Max pressure change: 2631656.573 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 268132.556 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.015532474243339062 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4460014709176576 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.68e+03 ) ( Rwell ) = ( 3.68e+02 ) ( R ) = ( 3.70e+03 ) + Last LinSolve(iter,res) = ( 10, 4.29e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00620539 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584313 s | Solve Time: 0.414339 s + compositionalMultiphaseFlow: Max pressure change: 4118230.686 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 393248.971 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4317638930310217 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.65e+03 ) ( Rwell ) = ( 3.64e+02 ) ( R ) = ( 3.66e+03 ) + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00325457 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588453 s | Solve Time: 0.332871 s + compositionalMultiphaseFlow: Max pressure change: 2700496.140 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 289662.883 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.029376721419406865 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8496211361161556 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.54e+03 ) ( Rwell ) = ( 3.53e+02 ) ( R ) = ( 3.55e+03 ) + Last LinSolve(iter,res) = ( 4, 3.25e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00999809 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585352 s | Solve Time: 1.1685 s + compositionalMultiphaseFlow: Max pressure change: 24176632.523 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 5737489.419 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 21.721555997091595 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.44e+03 ) ( Rwell ) = ( 3.50e+02 ) ( R ) = ( 3.46e+03 ) + Last LinSolve(iter,res) = ( 14, 1.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00715067 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59024 s | Solve Time: 1.34342 s + compositionalMultiphaseFlow: Max pressure change: 2543049.180 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 444304.542 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2831400110698112 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.41e+03 ) ( Rwell ) = ( 3.46e+02 ) ( R ) = ( 3.42e+03 ) + Last LinSolve(iter,res) = ( 16, 7.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00612936 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587083 s | Solve Time: 0.577291 s + compositionalMultiphaseFlow: Max pressure change: 1999720.090 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 311081.866 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7398858652373193 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.37e+03 ) ( Rwell ) = ( 3.43e+02 ) ( R ) = ( 3.39e+03 ) + Last LinSolve(iter,res) = ( 7, 6.13e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00493054 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586022 s | Solve Time: 1.08187 s + compositionalMultiphaseFlow: Max pressure change: 2056173.160 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 134665.743 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.010228830821962962 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5003417889106603 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.34e+03 ) ( Rwell ) = ( 3.39e+02 ) ( R ) = ( 3.35e+03 ) + Last LinSolve(iter,res) = ( 13, 4.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00966664 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587965 s | Solve Time: 0.997138 s + compositionalMultiphaseFlow: Max pressure change: 2011672.064 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 672666.915 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1063170451685334 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.30e+03 ) ( Rwell ) = ( 3.36e+02 ) ( R ) = ( 3.32e+03 ) + Last LinSolve(iter,res) = ( 12, 9.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00345437 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585963 s | Solve Time: 0.174686 s + compositionalMultiphaseFlow: Max pressure change: 2120341.213 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 256935.670 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5909944839611891 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.27e+03 ) ( Rwell ) = ( 3.33e+02 ) ( R ) = ( 3.28e+03 ) + Last LinSolve(iter,res) = ( 2, 3.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00559672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58628 s | Solve Time: 0.495042 s + compositionalMultiphaseFlow: Max pressure change: 2017873.647 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 260613.016 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01000284598675021 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5271942444485738 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.23e+03 ) ( Rwell ) = ( 3.29e+02 ) ( R ) = ( 3.25e+03 ) + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00799751 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58292 s | Solve Time: 0.253686 s + compositionalMultiphaseFlow: Max pressure change: 2251648.636 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 265318.510 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.978423301650067 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.20e+03 ) ( Rwell ) = ( 3.26e+02 ) ( R ) = ( 3.22e+03 ) + Last LinSolve(iter,res) = ( 3, 8.00e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00455684 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58909 s | Solve Time: 1.16746 s + compositionalMultiphaseFlow: Max pressure change: 1760204.468 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 112821.679 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.013212142985181403 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5013338407488133 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 20 + ( Rflow ) = ( 3.16e+03 ) ( Rwell ) = ( 3.22e+02 ) ( R ) = ( 3.17e+03 ) + Last LinSolve(iter,res) = ( 14, 4.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00256823 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586623 s | Solve Time: 1.34506 s + compositionalMultiphaseFlow: Max pressure change: 2342403.938 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 292284.926 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03619788850286075 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1882575256339223 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 21 + ( Rflow ) = ( 3.04e+03 ) ( Rwell ) = ( 3.10e+02 ) ( R ) = ( 3.05e+03 ) + Last LinSolve(iter,res) = ( 16, 2.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00283651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587926 s | Solve Time: 1.34504 s + compositionalMultiphaseFlow: Max pressure change: 1587121.660 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 98232.688 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.015019408886616875 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.4172981911280462 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 22 + ( Rflow ) = ( 2.99e+03 ) ( Rwell ) = ( 3.05e+02 ) ( R ) = ( 3.01e+03 ) + Last LinSolve(iter,res) = ( 16, 2.84e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.005856 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588065 s | Solve Time: 0.826717 s + compositionalMultiphaseFlow: Max pressure change: 1866548.016 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 174132.958 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.024560615848198554 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5480699812747076 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 23 + ( Rflow ) = ( 2.92e+03 ) ( Rwell ) = ( 2.98e+02 ) ( R ) = ( 2.94e+03 ) + Last LinSolve(iter,res) = ( 10, 5.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 17 | Final Rel Res: 0.00834922 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584822 s | Solve Time: 1.43366 s + compositionalMultiphaseFlow: Max pressure change: 3129980.750 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 370032.021 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01099295082306495 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7582589014811489 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 24 + ( Rflow ) = ( 2.89e+03 ) ( Rwell ) = ( 2.95e+02 ) ( R ) = ( 2.90e+03 ) + Last LinSolve(iter,res) = ( 17, 8.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 39 | Final Rel Res: 0.00367732 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587229 s | Solve Time: 3.54795 s + compositionalMultiphaseFlow: Max pressure change: 2352564.527 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 330786.773 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.02128655344507051 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.496272071165997 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 25 + ( Rflow ) = ( 2.82e+03 ) ( Rwell ) = ( 2.88e+02 ) ( R ) = ( 2.84e+03 ) + Last LinSolve(iter,res) = ( 39, 3.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.11206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588542 s | Solve Time: 29.0895 s + compositionalMultiphaseFlow: Max pressure change: 17039360.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2433225.676 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.785230724373985 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 26 + ( Rflow ) = ( 2.79e+03 ) ( Rwell ) = ( 2.86e+02 ) ( R ) = ( 2.81e+03 ) + Last LinSolve(iter,res) = ( 200, 1.12e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 53 | Final Rel Res: 0.00814258 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588322 s | Solve Time: 5.06613 s + compositionalMultiphaseFlow: Max pressure change: 1491812.561 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 260429.787 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9463800815484975 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 27 + ( Rflow ) = ( 2.77e+03 ) ( Rwell ) = ( 2.83e+02 ) ( R ) = ( 2.78e+03 ) + Last LinSolve(iter,res) = ( 53, 8.14e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 41 | Final Rel Res: 0.00816698 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587894 s | Solve Time: 3.7567 s + compositionalMultiphaseFlow: Max pressure change: 2459666.467 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 328387.110 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7884900985366268 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 28 + ( Rflow ) = ( 2.74e+03 ) ( Rwell ) = ( 2.80e+02 ) ( R ) = ( 2.75e+03 ) + Last LinSolve(iter,res) = ( 41, 8.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 49 | Final Rel Res: 0.00610292 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587524 s | Solve Time: 4.62061 s + compositionalMultiphaseFlow: Max pressure change: 1580796.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 239183.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.012107391951767008 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6322109069812862 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 29 + ( Rflow ) = ( 2.71e+03 ) ( Rwell ) = ( 2.76e+02 ) ( R ) = ( 2.72e+03 ) + Last LinSolve(iter,res) = ( 49, 6.10e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.010497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588069 s | Solve Time: 17.8538 s + compositionalMultiphaseFlow: Max pressure change: 1373824.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 191963.656 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6929351963962704 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 30 + ( Rflow ) = ( 2.68e+03 ) ( Rwell ) = ( 2.74e+02 ) ( R ) = ( 2.69e+03 ) + Last LinSolve(iter,res) = ( 200, 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 43 | Final Rel Res: 0.00976129 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589109 s | Solve Time: 3.97032 s + compositionalMultiphaseFlow: Max pressure change: 1575591.406 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 213606.662 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.4455129016505204 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 31 + ( Rflow ) = ( 2.65e+03 ) ( Rwell ) = ( 2.71e+02 ) ( R ) = ( 2.67e+03 ) + Last LinSolve(iter,res) = ( 43, 9.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 45 | Final Rel Res: 0.00752657 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589522 s | Solve Time: 4.1867 s + compositionalMultiphaseFlow: Max pressure change: 2065564.844 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 164175.547 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.010971268429341782 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.46785468035203337 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 32 + ( Rflow ) = ( 2.62e+03 ) ( Rwell ) = ( 2.68e+02 ) ( R ) = ( 2.64e+03 ) + Last LinSolve(iter,res) = ( 45, 7.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 56 | Final Rel Res: 0.00743999 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587953 s | Solve Time: 5.41073 s + compositionalMultiphaseFlow: Max pressure change: 2003523.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 216797.102 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6432642384357186 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 33 + ( Rflow ) = ( 2.59e+03 ) ( Rwell ) = ( 2.65e+02 ) ( R ) = ( 2.61e+03 ) + Last LinSolve(iter,res) = ( 56, 7.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.106976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.591752 s | Solve Time: 29.0407 s + compositionalMultiphaseFlow: Max pressure change: 21561344.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4118892.586 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 15.035250549492336 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 34 + ( Rflow ) = ( 2.57e+03 ) ( Rwell ) = ( 2.63e+02 ) ( R ) = ( 2.58e+03 ) + Last LinSolve(iter,res) = ( 200, 1.07e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.999483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590526 s | Solve Time: 29.0587 s + compositionalMultiphaseFlow: Max pressure change: 14680064.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 124234.451 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.011160739479379627 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.47081788820037207 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 35 + ( Rflow ) = ( 2.57e+03 ) ( Rwell ) = ( 2.63e+02 ) ( R ) = ( 2.58e+03 ) + Last LinSolve(iter,res) = ( 200, 9.99e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00366993 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58871 s | Solve Time: 1.08257 s + compositionalMultiphaseFlow: Max pressure change: 1857062.835 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 159483.973 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01327367595512147 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5547753228987773 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 36 + ( Rflow ) = ( 2.53e+03 ) ( Rwell ) = ( 2.59e+02 ) ( R ) = ( 2.55e+03 ) + Last LinSolve(iter,res) = ( 13, 3.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 20 | Final Rel Res: 0.0062825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58785 s | Solve Time: 1.70266 s + compositionalMultiphaseFlow: Max pressure change: 1124251.804 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 321771.084 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1889961443179453 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 37 + ( Rflow ) = ( 2.51e+03 ) ( Rwell ) = ( 2.57e+02 ) ( R ) = ( 2.52e+03 ) + Last LinSolve(iter,res) = ( 20, 6.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 25 | Final Rel Res: 0.00719434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590362 s | Solve Time: 2.16289 s + compositionalMultiphaseFlow: Max pressure change: 1461252.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 278971.320 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.025235643639772 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 38 + ( Rflow ) = ( 2.48e+03 ) ( Rwell ) = ( 2.54e+02 ) ( R ) = ( 2.50e+03 ) + Last LinSolve(iter,res) = ( 25, 7.19e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 19 | Final Rel Res: 0.00887266 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.592673 s | Solve Time: 1.61305 s + compositionalMultiphaseFlow: Max pressure change: 1972014.037 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 388292.879 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4117028749963598 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 39 + ( Rflow ) = ( 2.46e+03 ) ( Rwell ) = ( 2.52e+02 ) ( R ) = ( 2.47e+03 ) + Last LinSolve(iter,res) = ( 19, 8.87e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 25 | Final Rel Res: 0.00591893 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.592728 s | Solve Time: 2.16413 s + compositionalMultiphaseFlow: Max pressure change: 1115200.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 143484.164 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.38825068692381026 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 40 + ( Rflow ) = ( 2.43e+03 ) ( Rwell ) = ( 2.49e+02 ) ( R ) = ( 2.44e+03 ) + Last LinSolve(iter,res) = ( 25, 5.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.998368 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590752 s | Solve Time: 29.0403 s + compositionalMultiphaseFlow: Max pressure change: 233832448.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 192000.000 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.37947233351238374 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 41 + ( Rflow ) = ( 2.43e+03 ) ( Rwell ) = ( 2.49e+02 ) ( R ) = ( 2.44e+03 ) + Last LinSolve(iter,res) = ( 200, 9.98e-01 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.20740978272544086 + Line search @ 0.005: ( Rflow ) = ( 2.43e+03 ) ( Rwell ) = ( 2.49e+02 ) ( R ) = ( 2.44e+03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.11192736382803381 + Line search @ 0.003: ( Rflow ) = ( 2.43e+03 ) ( Rwell ) = ( 2.49e+02 ) ( R ) = ( 2.44e+03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.05825342563145397 + Line search @ 0.001: ( Rflow ) = ( 2.43e+03 ) ( Rwell ) = ( 2.49e+02 ) ( R ) = ( 2.44e+03 ) +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.029730025292336038 + Line search @ 0.001: ( Rflow ) = ( 2.43e+03 ) ( Rwell ) = ( 2.49e+02 ) ( R ) = ( 2.44e+03 ) + Line search failed to produce reduced residual. Accepting iteration. + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00149923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585875 s | Solve Time: 0.0960137 s + compositionalMultiphaseFlow: Max pressure change: 2039102.933 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 294746.783 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.19213705153671534 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.768409837070294 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 42 + ( Rflow ) = ( 1.93e+03 ) ( Rwell ) = ( 2.01e+02 ) ( R ) = ( 1.95e+03 ) + Last LinSolve(iter,res) = ( 1, 1.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.57566 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588261 s | Solve Time: 29.0658 s + compositionalMultiphaseFlow: Max pressure change: 67108864.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 8065024.000 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 24.186207672747997 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 43 + ( Rflow ) = ( 1.92e+03 ) ( Rwell ) = ( 2.00e+02 ) ( R ) = ( 1.93e+03 ) + Last LinSolve(iter,res) = ( 200, 5.76e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 88 | Final Rel Res: 0.00745583 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.592322 s | Solve Time: 9.48134 s + compositionalMultiphaseFlow: Max pressure change: 1600080.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 270972.594 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01850185551459686 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.46882128698835857 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 44 + ( Rflow ) = ( 1.88e+03 ) ( Rwell ) = ( 1.96e+02 ) ( R ) = ( 1.89e+03 ) + Last LinSolve(iter,res) = ( 88, 7.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.290586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589429 s | Solve Time: 29.0619 s + compositionalMultiphaseFlow: Max pressure change: 39321600.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2249450.125 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.163842929823463 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 45 + ( Rflow ) = ( 1.86e+03 ) ( Rwell ) = ( 1.94e+02 ) ( R ) = ( 1.87e+03 ) + Last LinSolve(iter,res) = ( 200, 2.91e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.252529 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.591349 s | Solve Time: 21.664 s + compositionalMultiphaseFlow: Max pressure change: 9373074.622 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1589733.596 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.179867097674629 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 46 + ( Rflow ) = ( 1.84e+03 ) ( Rwell ) = ( 1.92e+02 ) ( R ) = ( 1.85e+03 ) + Last LinSolve(iter,res) = ( 200, 2.53e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 43 | Final Rel Res: 0.00953117 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.593053 s | Solve Time: 3.9715 s + compositionalMultiphaseFlow: Max pressure change: 662855.812 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 230435.128 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.012805194679803577 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5352165367573665 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 47 + ( Rflow ) = ( 1.82e+03 ) ( Rwell ) = ( 1.90e+02 ) ( R ) = ( 1.83e+03 ) + Last LinSolve(iter,res) = ( 43, 9.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 64 | Final Rel Res: 0.00894432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589955 s | Solve Time: 6.35347 s + compositionalMultiphaseFlow: Max pressure change: 1003404.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 226038.500 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.021778472993578792 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.383499430962388 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 48 + ( Rflow ) = ( 1.78e+03 ) ( Rwell ) = ( 1.86e+02 ) ( R ) = ( 1.79e+03 ) + Last LinSolve(iter,res) = ( 64, 8.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 81 | Final Rel Res: 0.00970426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589894 s | Solve Time: 8.49899 s + compositionalMultiphaseFlow: Max pressure change: 996592.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 247703.594 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01117579155444751 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.45708653202802796 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 49 + ( Rflow ) = ( 1.76e+03 ) ( Rwell ) = ( 1.84e+02 ) ( R ) = ( 1.77e+03 ) + Last LinSolve(iter,res) = ( 81, 9.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | NotConverged | Iterations: 200 | Final Rel Res: 0.0210832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.591375 s | Solve Time: 22.0499 s + compositionalMultiphaseFlow: Max pressure change: 20873216.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4771882.000 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 15.536586832957271 +New dt = 2160000 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.25e+03 ) ( Rwell ) = ( 4.49e+02 ) ( R ) = ( 2.30e+03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00116949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582884 s | Solve Time: 0.0961476 s + compositionalMultiphaseFlow: Max pressure change: 3697674.774 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 156459.990 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.012882114452478444 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e+03 ) ( Rwell ) = ( 4.45e+02 ) ( R ) = ( 2.28e+03 ) + Last LinSolve(iter,res) = ( 1, 1.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00113658 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582809 s | Solve Time: 0.0964243 s + compositionalMultiphaseFlow: Max pressure change: 3623303.779 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 156242.792 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.4516355450648737 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e+03 ) ( Rwell ) = ( 4.40e+02 ) ( R ) = ( 2.25e+03 ) + Last LinSolve(iter,res) = ( 1, 1.14e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00117246 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579336 s | Solve Time: 0.0959159 s + compositionalMultiphaseFlow: Max pressure change: 3734996.155 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 155872.852 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.010093204047647334 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7048588814701355 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e+03 ) ( Rwell ) = ( 4.36e+02 ) ( R ) = ( 2.23e+03 ) + Last LinSolve(iter,res) = ( 1, 1.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00233428 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585124 s | Solve Time: 0.174861 s + compositionalMultiphaseFlow: Max pressure change: 4795442.146 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 240615.208 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0653136633625468 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.16e+03 ) ( Rwell ) = ( 4.31e+02 ) ( R ) = ( 2.21e+03 ) + Last LinSolve(iter,res) = ( 2, 2.33e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.0012995 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588031 s | Solve Time: 0.0960981 s + compositionalMultiphaseFlow: Max pressure change: 3554089.367 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 150782.671 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.023629776336424456 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.529364621296764 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e+03 ) ( Rwell ) = ( 4.21e+02 ) ( R ) = ( 2.15e+03 ) + Last LinSolve(iter,res) = ( 1, 1.30e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00120876 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587135 s | Solve Time: 0.174866 s + compositionalMultiphaseFlow: Max pressure change: 3469061.616 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 151934.556 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03514386313804005 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.190576923828135 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e+03 ) ( Rwell ) = ( 4.06e+02 ) ( R ) = ( 2.07e+03 ) + Last LinSolve(iter,res) = ( 2, 1.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00735932 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582792 s | Solve Time: 0.253432 s + compositionalMultiphaseFlow: Max pressure change: 2337129.183 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 183370.759 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6814067011266265 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.01e+03 ) ( Rwell ) = ( 4.02e+02 ) ( R ) = ( 2.05e+03 ) + Last LinSolve(iter,res) = ( 3, 7.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00218688 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585821 s | Solve Time: 0.494927 s + compositionalMultiphaseFlow: Max pressure change: 2730828.074 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 138228.925 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.04361832593464102 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.40422917471028 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.92e+03 ) ( Rwell ) = ( 3.85e+02 ) ( R ) = ( 1.96e+03 ) + Last LinSolve(iter,res) = ( 6, 2.19e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00115189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583065 s | Solve Time: 0.414361 s + compositionalMultiphaseFlow: Max pressure change: 2170500.104 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 94673.037 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.09265031780850834 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.266815992984057 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.75e+03 ) ( Rwell ) = ( 3.49e+02 ) ( R ) = ( 1.78e+03 ) + Last LinSolve(iter,res) = ( 5, 1.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00837547 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587628 s | Solve Time: 0.413965 s + compositionalMultiphaseFlow: Max pressure change: 2070718.928 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 144414.484 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.011802824192008315 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5522816744643269 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.73e+03 ) ( Rwell ) = ( 3.45e+02 ) ( R ) = ( 1.76e+03 ) + Last LinSolve(iter,res) = ( 5, 8.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00133045 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586661 s | Solve Time: 0.253588 s + compositionalMultiphaseFlow: Max pressure change: 2940512.422 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 143484.407 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.11752308472631935 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.087702085357991 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e+03 ) ( Rwell ) = ( 3.04e+02 ) ( R ) = ( 1.54e+03 ) + Last LinSolve(iter,res) = ( 3, 1.33e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 19 | Final Rel Res: 0.00266687 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582399 s | Solve Time: 1.60918 s + compositionalMultiphaseFlow: Max pressure change: 2830536.272 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 159210.907 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.035145652613284416 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5090554208531763 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.46e+03 ) ( Rwell ) = ( 2.94e+02 ) ( R ) = ( 1.49e+03 ) + Last LinSolve(iter,res) = ( 19, 2.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 31 | Final Rel Res: 0.00904034 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585732 s | Solve Time: 2.74077 s + compositionalMultiphaseFlow: Max pressure change: 2934046.209 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 163677.895 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.010619873177019427 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5002011197528882 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.44e+03 ) ( Rwell ) = ( 2.91e+02 ) ( R ) = ( 1.47e+03 ) + Last LinSolve(iter,res) = ( 31, 9.04e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00884577 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589229 s | Solve Time: 1.08188 s + compositionalMultiphaseFlow: Max pressure change: 2541047.071 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 178268.357 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6468911431723305 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.43e+03 ) ( Rwell ) = ( 2.88e+02 ) ( R ) = ( 1.46e+03 ) + Last LinSolve(iter,res) = ( 13, 8.85e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00707042 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586449 s | Solve Time: 0.742306 s + compositionalMultiphaseFlow: Max pressure change: 2445306.637 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 137985.713 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.013042797539582584 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.4133664483461672 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.41e+03 ) ( Rwell ) = ( 2.84e+02 ) ( R ) = ( 1.44e+03 ) + Last LinSolve(iter,res) = ( 9, 7.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00452837 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586478 s | Solve Time: 0.742532 s + compositionalMultiphaseFlow: Max pressure change: 1833212.130 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 143534.762 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.08265444705519644 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6852261824859376 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.29e+03 ) ( Rwell ) = ( 2.61e+02 ) ( R ) = ( 1.31e+03 ) + Last LinSolve(iter,res) = ( 9, 4.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00565782 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586489 s | Solve Time: 1.34373 s + compositionalMultiphaseFlow: Max pressure change: 1439637.129 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 136939.874 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.010155033114743112 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.2973018349635268 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.27e+03 ) ( Rwell ) = ( 2.58e+02 ) ( R ) = ( 1.30e+03 ) + Last LinSolve(iter,res) = ( 16, 5.66e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0062253 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589651 s | Solve Time: 0.495111 s + compositionalMultiphaseFlow: Max pressure change: 1391101.186 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 123256.592 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.011175054926017381 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.28245979861182136 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.26e+03 ) ( Rwell ) = ( 2.55e+02 ) ( R ) = ( 1.28e+03 ) + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00521141 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588031 s | Solve Time: 0.741939 s + compositionalMultiphaseFlow: Max pressure change: 2574574.748 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 141645.269 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01018874835035999 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5004496785822621 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.25e+03 ) ( Rwell ) = ( 2.52e+02 ) ( R ) = ( 1.27e+03 ) + Last LinSolve(iter,res) = ( 9, 5.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00485841 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586306 s | Solve Time: 0.417449 s + compositionalMultiphaseFlow: Max pressure change: 1491877.380 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 88979.683 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.02873771702108673 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7619806125448072 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 20 + ( Rflow ) = ( 1.21e+03 ) ( Rwell ) = ( 2.45e+02 ) ( R ) = ( 1.23e+03 ) + Last LinSolve(iter,res) = ( 5, 4.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 15 | Final Rel Res: 0.004167 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585955 s | Solve Time: 1.25566 s + compositionalMultiphaseFlow: Max pressure change: 2011218.896 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 143943.474 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.024713127337226325 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.66436497492721 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 21 + ( Rflow ) = ( 1.18e+03 ) ( Rwell ) = ( 2.39e+02 ) ( R ) = ( 1.20e+03 ) + Last LinSolve(iter,res) = ( 15, 4.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 19 | Final Rel Res: 0.00272941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588098 s | Solve Time: 1.61218 s + compositionalMultiphaseFlow: Max pressure change: 1848097.438 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 138884.924 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.042439613770611485 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.015943341938769 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 22 + ( Rflow ) = ( 1.12e+03 ) ( Rwell ) = ( 2.29e+02 ) ( R ) = ( 1.15e+03 ) + Last LinSolve(iter,res) = ( 19, 2.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00981816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582802 s | Solve Time: 0.91071 s + compositionalMultiphaseFlow: Max pressure change: 1798281.207 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 216690.351 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7856731641589347 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 23 + ( Rflow ) = ( 1.11e+03 ) ( Rwell ) = ( 2.27e+02 ) ( R ) = ( 1.13e+03 ) + Last LinSolve(iter,res) = ( 11, 9.82e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00509812 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588116 s | Solve Time: 0.826355 s + compositionalMultiphaseFlow: Max pressure change: 1798517.352 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 154699.906 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.028734101123083187 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7947557584941656 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 24 + ( Rflow ) = ( 1.08e+03 ) ( Rwell ) = ( 2.20e+02 ) ( R ) = ( 1.10e+03 ) + Last LinSolve(iter,res) = ( 10, 5.10e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00450202 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5851 s | Solve Time: 1.16891 s + compositionalMultiphaseFlow: Max pressure change: 1992061.976 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 129145.256 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0211655984640166 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5065556544693581 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 25 + ( Rflow ) = ( 1.05e+03 ) ( Rwell ) = ( 2.15e+02 ) ( R ) = ( 1.07e+03 ) + Last LinSolve(iter,res) = ( 14, 4.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00617342 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58552 s | Solve Time: 1.34358 s + compositionalMultiphaseFlow: Max pressure change: 1352065.215 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 114668.824 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.037921817443014205 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5167117389736755 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 26 + ( Rflow ) = ( 1.01e+03 ) ( Rwell ) = ( 2.07e+02 ) ( R ) = ( 1.03e+03 ) + Last LinSolve(iter,res) = ( 16, 6.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.0097372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589829 s | Solve Time: 0.827114 s + compositionalMultiphaseFlow: Max pressure change: 1807942.715 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 197972.595 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6101951820520435 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 27 + ( Rflow ) = ( 1.00e+03 ) ( Rwell ) = ( 2.05e+02 ) ( R ) = ( 1.02e+03 ) + Last LinSolve(iter,res) = ( 10, 9.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00349501 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585872 s | Solve Time: 0.414295 s + compositionalMultiphaseFlow: Max pressure change: 1988655.671 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 133894.112 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.06971008272887706 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2039880311593123 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 28 + ( Rflow ) = ( 9.26e+02 ) ( Rwell ) = ( 1.91e+02 ) ( R ) = ( 9.45e+02 ) + Last LinSolve(iter,res) = ( 5, 3.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00196072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585548 s | Solve Time: 0.658842 s + compositionalMultiphaseFlow: Max pressure change: 1484633.850 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 138481.831 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.09478191444076835 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5850905117971728 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 29 + ( Rflow ) = ( 8.32e+02 ) ( Rwell ) = ( 1.73e+02 ) ( R ) = ( 8.50e+02 ) + Last LinSolve(iter,res) = ( 8, 1.96e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00213737 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587933 s | Solve Time: 0.741902 s + compositionalMultiphaseFlow: Max pressure change: 904918.715 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 86631.008 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.08237661488155563 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3751833771288418 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 30 + ( Rflow ) = ( 7.60e+02 ) ( Rwell ) = ( 1.59e+02 ) ( R ) = ( 7.77e+02 ) + Last LinSolve(iter,res) = ( 9, 2.14e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 19 | Final Rel Res: 0.00948884 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58719 s | Solve Time: 1.61147 s + compositionalMultiphaseFlow: Max pressure change: 1317763.004 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 141739.707 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.014025208533139544 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.2197702677058091 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 31 + ( Rflow ) = ( 7.49e+02 ) ( Rwell ) = ( 1.56e+02 ) ( R ) = ( 7.65e+02 ) + Last LinSolve(iter,res) = ( 19, 9.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00105579 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582584 s | Solve Time: 0.742764 s + compositionalMultiphaseFlow: Max pressure change: 1413419.748 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 138670.143 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.2104540483245095 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5122014072889485 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 32 + ( Rflow ) = ( 5.75e+02 ) ( Rwell ) = ( 1.23e+02 ) ( R ) = ( 5.88e+02 ) + Last LinSolve(iter,res) = ( 9, 1.06e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 27 | Final Rel Res: 0.00789925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586731 s | Solve Time: 2.35481 s + compositionalMultiphaseFlow: Max pressure change: 1022635.317 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 100556.937 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03431462142714885 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2288483570520299 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 33 + ( Rflow ) = ( 5.55e+02 ) ( Rwell ) = ( 1.19e+02 ) ( R ) = ( 5.68e+02 ) + Last LinSolve(iter,res) = ( 27, 7.90e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 23 | Final Rel Res: 0.0033634 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585595 s | Solve Time: 1.97883 s + compositionalMultiphaseFlow: Max pressure change: 944400.221 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 96846.293 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.07772207252723964 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6312955732147074 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 34 + ( Rflow ) = ( 5.12e+02 ) ( Rwell ) = ( 1.10e+02 ) ( R ) = ( 5.24e+02 ) + Last LinSolve(iter,res) = ( 23, 3.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00383114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584211 s | Solve Time: 0.74241 s + compositionalMultiphaseFlow: Max pressure change: 897444.646 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 90677.944 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03696051592942618 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.161161010726854 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 35 + ( Rflow ) = ( 4.93e+02 ) ( Rwell ) = ( 1.06e+02 ) ( R ) = ( 5.04e+02 ) + Last LinSolve(iter,res) = ( 9, 3.83e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.0030955 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.593603 s | Solve Time: 0.99701 s + compositionalMultiphaseFlow: Max pressure change: 911330.268 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 87444.597 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.08338754434037518 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5093421080037963 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 36 + ( Rflow ) = ( 4.52e+02 ) ( Rwell ) = ( 9.71e+01 ) ( R ) = ( 4.62e+02 ) + Last LinSolve(iter,res) = ( 12, 3.10e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00858592 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587949 s | Solve Time: 1.34348 s + compositionalMultiphaseFlow: Max pressure change: 784798.787 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 82406.133 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03094100746417101 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.8599747172227197 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 37 + ( Rflow ) = ( 4.38e+02 ) ( Rwell ) = ( 9.41e+01 ) ( R ) = ( 4.48e+02 ) + Last LinSolve(iter,res) = ( 16, 8.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00776844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585173 s | Solve Time: 0.742309 s + compositionalMultiphaseFlow: Max pressure change: 607441.517 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 82208.839 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.020663164886661277 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5574540027825812 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 38 + ( Rflow ) = ( 4.29e+02 ) ( Rwell ) = ( 9.21e+01 ) ( R ) = ( 4.39e+02 ) + Last LinSolve(iter,res) = ( 9, 7.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00516487 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590176 s | Solve Time: 0.494076 s + compositionalMultiphaseFlow: Max pressure change: 682861.770 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 79712.208 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03004138336778518 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7929466019205513 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 39 + ( Rflow ) = ( 4.16e+02 ) ( Rwell ) = ( 8.94e+01 ) ( R ) = ( 4.26e+02 ) + Last LinSolve(iter,res) = ( 6, 5.16e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00468167 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585523 s | Solve Time: 0.333003 s + compositionalMultiphaseFlow: Max pressure change: 572599.761 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 78742.965 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.03548089431906879 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9084994292728439 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 40 + ( Rflow ) = ( 4.01e+02 ) ( Rwell ) = ( 8.62e+01 ) ( R ) = ( 4.10e+02 ) + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00393584 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588935 s | Solve Time: 0.495309 s + compositionalMultiphaseFlow: Max pressure change: 661919.978 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 75095.874 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.053326401705613036 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3145931030818474 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 41 + ( Rflow ) = ( 3.80e+02 ) ( Rwell ) = ( 8.16e+01 ) ( R ) = ( 3.89e+02 ) + Last LinSolve(iter,res) = ( 6, 3.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00860922 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585913 s | Solve Time: 0.994869 s + compositionalMultiphaseFlow: Max pressure change: 602844.612 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 71967.354 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.025168887955635336 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5890236800058979 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 42 + ( Rflow ) = ( 3.70e+02 ) ( Rwell ) = ( 7.95e+01 ) ( R ) = ( 3.79e+02 ) + Last LinSolve(iter,res) = ( 12, 8.61e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00948913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585514 s | Solve Time: 0.660145 s + compositionalMultiphaseFlow: Max pressure change: 723442.116 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 69008.553 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.02481228611136325 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.565884771627406 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 43 + ( Rflow ) = ( 3.61e+02 ) ( Rwell ) = ( 7.76e+01 ) ( R ) = ( 3.69e+02 ) + Last LinSolve(iter,res) = ( 8, 9.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00293286 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589096 s | Solve Time: 0.658825 s + compositionalMultiphaseFlow: Max pressure change: 573930.428 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 68940.058 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.07937796019315914 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7594219450603141 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 44 + ( Rflow ) = ( 3.33e+02 ) ( Rwell ) = ( 7.14e+01 ) ( R ) = ( 3.40e+02 ) + Last LinSolve(iter,res) = ( 8, 2.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00914641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584605 s | Solve Time: 0.828618 s + compositionalMultiphaseFlow: Max pressure change: 487900.094 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 64572.264 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0559413174198607 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.144698261998652 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 45 + ( Rflow ) = ( 3.14e+02 ) ( Rwell ) = ( 6.74e+01 ) ( R ) = ( 3.21e+02 ) + Last LinSolve(iter,res) = ( 10, 9.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00452124 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588838 s | Solve Time: 0.995835 s + compositionalMultiphaseFlow: Max pressure change: 468864.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 61287.250 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.04505896848540118 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.8713906636870554 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 46 + ( Rflow ) = ( 3.00e+02 ) ( Rwell ) = ( 6.44e+01 ) ( R ) = ( 3.07e+02 ) + Last LinSolve(iter,res) = ( 12, 4.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00301802 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583198 s | Solve Time: 0.996612 s + compositionalMultiphaseFlow: Max pressure change: 520761.666 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 58205.623 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.08036642179834112 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4804491768231784 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 47 + ( Rflow ) = ( 2.76e+02 ) ( Rwell ) = ( 5.92e+01 ) ( R ) = ( 2.82e+02 ) + Last LinSolve(iter,res) = ( 12, 3.02e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00451535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582721 s | Solve Time: 1.16822 s + compositionalMultiphaseFlow: Max pressure change: 508141.171 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53862.003 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.05566910741421189 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9451488163018453 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 48 + ( Rflow ) = ( 2.60e+02 ) ( Rwell ) = ( 5.59e+01 ) ( R ) = ( 2.66e+02 ) + Last LinSolve(iter,res) = ( 14, 4.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00150606 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584631 s | Solve Time: 0.175051 s + compositionalMultiphaseFlow: Max pressure change: 425751.593 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51625.707 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.2028441335389482 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2291568168205433 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 49 + ( Rflow ) = ( 2.08e+02 ) ( Rwell ) = ( 4.46e+01 ) ( R ) = ( 2.13e+02 ) + Last LinSolve(iter,res) = ( 2, 1.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 15 | Final Rel Res: 0.00433724 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582991 s | Solve Time: 1.25473 s + compositionalMultiphaseFlow: Max pressure change: 380177.993 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41845.366 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.25680013715133393 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.263476889434278 +New dt = 1080000 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e+03 ) ( Rwell ) = ( 4.49e+02 ) ( R ) = ( 1.21e+03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00110222 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583457 s | Solve Time: 0.0960189 s + compositionalMultiphaseFlow: Max pressure change: 3655694.612 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 78365.219 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.012481315336803677 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.005022455999952102 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e+03 ) ( Rwell ) = ( 4.44e+02 ) ( R ) = ( 1.20e+03 ) + Last LinSolve(iter,res) = ( 1, 1.10e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00107506 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580342 s | Solve Time: 0.0965891 s + compositionalMultiphaseFlow: Max pressure change: 3588684.977 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 78124.631 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.013069277396946077 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.01247527071204102 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e+03 ) ( Rwell ) = ( 4.38e+02 ) ( R ) = ( 1.18e+03 ) + Last LinSolve(iter,res) = ( 1, 1.08e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00107137 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.579997 s | Solve Time: 0.0962321 s + compositionalMultiphaseFlow: Max pressure change: 3504841.760 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 77390.778 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.013906520852176177 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.4090630493730827 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e+03 ) ( Rwell ) = ( 4.32e+02 ) ( R ) = ( 1.17e+03 ) + Last LinSolve(iter,res) = ( 1, 1.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00734099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588502 s | Solve Time: 0.253455 s + compositionalMultiphaseFlow: Max pressure change: 3634034.455 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 109988.042 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01406905267845173 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.07818753596546868 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e+03 ) ( Rwell ) = ( 4.26e+02 ) ( R ) = ( 1.15e+03 ) + Last LinSolve(iter,res) = ( 3, 7.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.0017219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590054 s | Solve Time: 0.826535 s + compositionalMultiphaseFlow: Max pressure change: 3543334.098 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 79648.333 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.019379011618134982 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.06215899019935356 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.05e+03 ) ( Rwell ) = ( 4.17e+02 ) ( R ) = ( 1.13e+03 ) + Last LinSolve(iter,res) = ( 10, 1.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00761559 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58267 s | Solve Time: 0.576938 s + compositionalMultiphaseFlow: Max pressure change: 3229576.271 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 133697.699 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.012150404358958568 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6293869103569407 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e+03 ) ( Rwell ) = ( 4.12e+02 ) ( R ) = ( 1.11e+03 ) + Last LinSolve(iter,res) = ( 7, 7.62e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00154337 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585094 s | Solve Time: 0.659063 s + compositionalMultiphaseFlow: Max pressure change: 3471698.943 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 76789.727 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.030703421127542797 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9859857796696532 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.00e+03 ) ( Rwell ) = ( 4.00e+02 ) ( R ) = ( 1.08e+03 ) + Last LinSolve(iter,res) = ( 8, 1.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00415238 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583138 s | Solve Time: 0.693519 s + compositionalMultiphaseFlow: Max pressure change: 3580029.185 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 69001.159 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.051253646156532516 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3858071326016472 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.48e+02 ) ( Rwell ) = ( 3.79e+02 ) ( R ) = ( 1.02e+03 ) + Last LinSolve(iter,res) = ( 8, 4.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.0049022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58236 s | Solve Time: 0.826456 s + compositionalMultiphaseFlow: Max pressure change: 3280326.583 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 77731.888 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.020800840884253474 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6018776783344659 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.27e+02 ) ( Rwell ) = ( 3.71e+02 ) ( R ) = ( 9.99e+02 ) + Last LinSolve(iter,res) = ( 10, 4.90e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00611363 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584625 s | Solve Time: 0.659854 s + compositionalMultiphaseFlow: Max pressure change: 4213212.257 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26832.205 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.05386125729290352 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5327408727070384 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.78e+02 ) ( Rwell ) = ( 3.51e+02 ) ( R ) = ( 9.45e+02 ) + Last LinSolve(iter,res) = ( 8, 6.11e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 47 | Final Rel Res: 0.00991502 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.597723 s | Solve Time: 4.39867 s + compositionalMultiphaseFlow: Max pressure change: 2798655.228 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 92553.939 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01488407069312571 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5012349635334787 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.65e+02 ) ( Rwell ) = ( 3.46e+02 ) ( R ) = ( 9.31e+02 ) + Last LinSolve(iter,res) = ( 47, 9.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 27 | Final Rel Res: 0.00747066 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588672 s | Solve Time: 2.35203 s + compositionalMultiphaseFlow: Max pressure change: 2784809.455 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 85683.415 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01613045426524344 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5019450659303224 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.50e+02 ) ( Rwell ) = ( 3.40e+02 ) ( R ) = ( 9.16e+02 ) + Last LinSolve(iter,res) = ( 27, 7.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 20 | Final Rel Res: 0.0039331 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586519 s | Solve Time: 1.69966 s + compositionalMultiphaseFlow: Max pressure change: 2569982.838 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 67728.436 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.025744525534395088 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5772564798144373 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.28e+02 ) ( Rwell ) = ( 3.32e+02 ) ( R ) = ( 8.92e+02 ) + Last LinSolve(iter,res) = ( 20, 3.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 19 | Final Rel Res: 0.00429326 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583141 s | Solve Time: 1.61239 s + compositionalMultiphaseFlow: Max pressure change: 2427072.740 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 89098.665 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.015654833634638196 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5101532124750368 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.14e+02 ) ( Rwell ) = ( 3.26e+02 ) ( R ) = ( 8.77e+02 ) + Last LinSolve(iter,res) = ( 19, 4.29e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00850555 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588282 s | Solve Time: 0.996348 s + compositionalMultiphaseFlow: Max pressure change: 1613174.582 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 193007.888 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.7000091667627621 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.06e+02 ) ( Rwell ) = ( 3.23e+02 ) ( R ) = ( 8.68e+02 ) + Last LinSolve(iter,res) = ( 12, 8.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.0097585 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590985 s | Solve Time: 1.1682 s + compositionalMultiphaseFlow: Max pressure change: 19975714.782 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1099884.354 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.01 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.943628273804868 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.87e+02 ) ( Rwell ) = ( 3.20e+02 ) ( R ) = ( 8.50e+02 ) + Last LinSolve(iter,res) = ( 14, 9.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00441326 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587933 s | Solve Time: 1.08307 s + compositionalMultiphaseFlow: Max pressure change: 2068394.125 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 71038.902 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.030929369979330795 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5364136537452531 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.62e+02 ) ( Rwell ) = ( 3.10e+02 ) ( R ) = ( 8.23e+02 ) + Last LinSolve(iter,res) = ( 13, 4.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.0076288 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584929 s | Solve Time: 0.911204 s + compositionalMultiphaseFlow: Max pressure change: 2474434.117 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38581.471 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0398406422826531 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5574937052596958 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 7.32e+02 ) ( Rwell ) = ( 2.98e+02 ) ( R ) = ( 7.90e+02 ) + Last LinSolve(iter,res) = ( 11, 7.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00327646 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583626 s | Solve Time: 0.659073 s + compositionalMultiphaseFlow: Max pressure change: 2082543.638 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66497.268 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.040733585958940464 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5828189231883147 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 7.01e+02 ) ( Rwell ) = ( 2.86e+02 ) ( R ) = ( 7.57e+02 ) + Last LinSolve(iter,res) = ( 8, 3.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00268389 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589258 s | Solve Time: 0.996935 s + compositionalMultiphaseFlow: Max pressure change: 1399587.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25879.690 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0855394164676179 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5357648304255209 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 20 + ( Rflow ) = ( 6.41e+02 ) ( Rwell ) = ( 2.61e+02 ) ( R ) = ( 6.92e+02 ) + Last LinSolve(iter,res) = ( 12, 2.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 21 | Final Rel Res: 0.00444702 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588735 s | Solve Time: 1.7954 s + compositionalMultiphaseFlow: Max pressure change: 1952481.808 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66949.641 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.051717108174873266 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.6543717456533553 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 21 + ( Rflow ) = ( 6.06e+02 ) ( Rwell ) = ( 2.48e+02 ) ( R ) = ( 6.55e+02 ) + Last LinSolve(iter,res) = ( 21, 4.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 25 | Final Rel Res: 0.00644004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586209 s | Solve Time: 2.16816 s + compositionalMultiphaseFlow: Max pressure change: 1709736.947 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 93762.932 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.014874479533331725 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.12475818567641284 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 22 + ( Rflow ) = ( 5.97e+02 ) ( Rwell ) = ( 2.44e+02 ) ( R ) = ( 6.45e+02 ) + Last LinSolve(iter,res) = ( 25, 6.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00217826 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584878 s | Solve Time: 0.662123 s + compositionalMultiphaseFlow: Max pressure change: 1321437.336 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43002.877 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.15405845753501385 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8801897308831457 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 23 + ( Rflow ) = ( 5.03e+02 ) ( Rwell ) = ( 2.06e+02 ) ( R ) = ( 5.43e+02 ) + Last LinSolve(iter,res) = ( 8, 2.18e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00269147 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585982 s | Solve Time: 1.09369 s + compositionalMultiphaseFlow: Max pressure change: 1696188.798 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66135.967 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.06671978606679313 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5850114144074734 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 24 + ( Rflow ) = ( 4.67e+02 ) ( Rwell ) = ( 1.93e+02 ) ( R ) = ( 5.05e+02 ) + Last LinSolve(iter,res) = ( 13, 2.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00621994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.592378 s | Solve Time: 0.827932 s + compositionalMultiphaseFlow: Max pressure change: 1299809.167 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 67890.735 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.04096562468903955 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5374223248570629 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 25 + ( Rflow ) = ( 4.46e+02 ) ( Rwell ) = ( 1.85e+02 ) ( R ) = ( 4.83e+02 ) + Last LinSolve(iter,res) = ( 10, 6.22e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00569618 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.591866 s | Solve Time: 0.414612 s + compositionalMultiphaseFlow: Max pressure change: 1255641.416 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 69128.018 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.05470607216835328 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.49760615188144586 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 26 + ( Rflow ) = ( 4.20e+02 ) ( Rwell ) = ( 1.75e+02 ) ( R ) = ( 4.55e+02 ) + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00608149 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586793 s | Solve Time: 1.17056 s + compositionalMultiphaseFlow: Max pressure change: 861002.659 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50031.489 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.030827782776420624 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5582416993282755 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 27 + ( Rflow ) = ( 4.07e+02 ) ( Rwell ) = ( 1.69e+02 ) ( R ) = ( 4.40e+02 ) + Last LinSolve(iter,res) = ( 14, 6.08e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00969538 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589914 s | Solve Time: 0.659905 s + compositionalMultiphaseFlow: Max pressure change: 1436440.416 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 71743.730 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.054170635098502826 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5324482751494097 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 28 + ( Rflow ) = ( 3.83e+02 ) ( Rwell ) = ( 1.60e+02 ) ( R ) = ( 4.15e+02 ) + Last LinSolve(iter,res) = ( 8, 9.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.0027128 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583229 s | Solve Time: 0.997412 s + compositionalMultiphaseFlow: Max pressure change: 1348932.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 68332.071 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.1486983985485469 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.935926894943858 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 29 + ( Rflow ) = ( 3.21e+02 ) ( Rwell ) = ( 1.36e+02 ) ( R ) = ( 3.48e+02 ) + Last LinSolve(iter,res) = ( 12, 2.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 19 | Final Rel Res: 0.00499193 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585298 s | Solve Time: 1.61615 s + compositionalMultiphaseFlow: Max pressure change: 893063.794 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46052.269 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.05608626853668795 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9211692030221847 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 30 + ( Rflow ) = ( 3.03e+02 ) ( Rwell ) = ( 1.29e+02 ) ( R ) = ( 3.29e+02 ) + Last LinSolve(iter,res) = ( 19, 4.99e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00582848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588065 s | Solve Time: 0.914625 s + compositionalMultiphaseFlow: Max pressure change: 872635.982 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45781.788 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0347479704106288 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5407097680699131 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 31 + ( Rflow ) = ( 2.92e+02 ) ( Rwell ) = ( 1.24e+02 ) ( R ) = ( 3.17e+02 ) + Last LinSolve(iter,res) = ( 11, 5.83e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00919099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582928 s | Solve Time: 0.494484 s + compositionalMultiphaseFlow: Max pressure change: 842870.238 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 57055.889 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.0280869694270667 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.5152917551600624 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 32 + ( Rflow ) = ( 2.84e+02 ) ( Rwell ) = ( 1.21e+02 ) ( R ) = ( 3.09e+02 ) + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00507274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583959 s | Solve Time: 0.66054 s + compositionalMultiphaseFlow: Max pressure change: 909145.984 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42739.107 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.07438986530691426 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0809333563546488 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 33 + ( Rflow ) = ( 2.63e+02 ) ( Rwell ) = ( 1.12e+02 ) ( R ) = ( 2.86e+02 ) + Last LinSolve(iter,res) = ( 8, 5.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00133258 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588011 s | Solve Time: 0.741143 s + compositionalMultiphaseFlow: Max pressure change: 770608.525 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40520.043 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.1998390804502433 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6598650516789597 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 34 + ( Rflow ) = ( 2.10e+02 ) ( Rwell ) = ( 8.94e+01 ) ( R ) = ( 2.29e+02 ) + Last LinSolve(iter,res) = ( 9, 1.33e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00295385 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583821 s | Solve Time: 0.494254 s + compositionalMultiphaseFlow: Max pressure change: 601496.013 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33487.520 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.12102678779097362 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3093017932074353 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 35 + ( Rflow ) = ( 1.85e+02 ) ( Rwell ) = ( 7.86e+01 ) ( R ) = ( 2.01e+02 ) + Last LinSolve(iter,res) = ( 6, 2.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00106464 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58644 s | Solve Time: 0.910611 s + compositionalMultiphaseFlow: Max pressure change: 541296.363 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29818.339 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.5947633699001729 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.487994354373677 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 36 + ( Rflow ) = ( 7.55e+01 ) ( Rwell ) = ( 3.18e+01 ) ( R ) = ( 8.19e+01 ) + Last LinSolve(iter,res) = ( 11, 1.06e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00762508 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582356 s | Solve Time: 1.16771 s + compositionalMultiphaseFlow: Max pressure change: 208450.299 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13370.857 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.2358164228649738 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9663563345917767 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 37 + ( Rflow ) = ( 5.78e+01 ) ( Rwell ) = ( 2.43e+01 ) ( R ) = ( 6.27e+01 ) + Last LinSolve(iter,res) = ( 14, 7.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00126012 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58378 s | Solve Time: 0.825509 s + compositionalMultiphaseFlow: Max pressure change: 187418.234 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 10352.918 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 0.7013295440640895 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1784209878439924 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 38 + ( Rflow ) = ( 1.73e+01 ) ( Rwell ) = ( 7.27e+00 ) ( R ) = ( 1.88e+01 ) + Last LinSolve(iter,res) = ( 10, 1.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00381887 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585317 s | Solve Time: 0.333707 s + compositionalMultiphaseFlow: Max pressure change: 53018.139 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3373.336 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.9720631750662478 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 39 + ( Rflow ) = ( 1.17e-01 ) ( Rwell ) = ( 6.19e-05 ) ( R ) = ( 1.17e-01 ) + Last LinSolve(iter,res) = ( 4, 3.82e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00422744 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584391 s | Solve Time: 0.826287 s + compositionalMultiphaseFlow: Max pressure change: 14142.876 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 300.712 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0761290663310672 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 40 + ( Rflow ) = ( 2.46e-02 ) ( Rwell ) = ( 1.85e-08 ) ( R ) = ( 2.46e-02 ) + Last LinSolve(iter,res) = ( 10, 4.23e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00362317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581839 s | Solve Time: 0.25363 s + compositionalMultiphaseFlow: Max pressure change: 1194.394 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 67.044 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.02464636896189698 + Attempt: 2, ConfigurationIter: 0, NewtonIter: 41 + ( Rflow ) = ( 1.63e-05 ) ( Rwell ) = ( 3.24e-12 ) ( R ) = ( 1.63e-05 ) + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13171366.954792757 Pa +wellControls2: Total rate: 491.5779228071055 mol/s; total surface volumetric rate: 11.574074074036586 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.574074074036586 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 55.177 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Time-step required will be decreased based on state change. +reservoirSystem: sub-step = 0, accepted dt = 1080000, remaining dt = 3240000 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-01 ) ( Rwell ) = ( 7.71e-09 ) ( R ) = ( 2.73e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00568274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583622 s | Solve Time: 0.25407 s + compositionalMultiphaseFlow: Max pressure change: 74437.623 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 631.730 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0018478575445342038 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.45e-03 ) ( Rwell ) = ( 1.03e-08 ) ( R ) = ( 8.45e-03 ) + Last LinSolve(iter,res) = ( 3, 5.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00210114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58158 s | Solve Time: 0.253599 s + compositionalMultiphaseFlow: Max pressure change: 1573.987 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 17.550 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0018458328133279522 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-05 ) ( Rwell ) = ( 1.17e-11 ) ( R ) = ( 3.11e-05 ) + Last LinSolve(iter,res) = ( 3, 2.10e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13250244.70037571 Pa +wellControls2: Total rate: 491.5779228086976 mol/s; total surface volumetric rate: 11.574074074074073 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.574074074074073 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.776 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +reservoirSystem: sub-step = 1, accepted dt = 497105.95517404994, remaining dt = 2742894.04482595 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-01 ) ( Rwell ) = ( 5.66e-10 ) ( R ) = ( 3.16e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00746297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582127 s | Solve Time: 0.253521 s + compositionalMultiphaseFlow: Max pressure change: 36475.461 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 766.992 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00243270769873849 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.74e-03 ) ( Rwell ) = ( 2.05e-09 ) ( R ) = ( 2.74e-03 ) + Last LinSolve(iter,res) = ( 3, 7.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00907279 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589992 s | Solve Time: 0.253574 s + compositionalMultiphaseFlow: Max pressure change: 1235.416 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 9.654 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0024254049278586987 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-05 ) ( Rwell ) = ( 9.20e-12 ) ( R ) = ( 2.69e-05 ) + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13285533.243550314 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.394 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +reservoirSystem: sub-step = 2, accepted dt = 994211.9103480999, remaining dt = 1748682.1344778503 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-01 ) ( Rwell ) = ( 1.32e-10 ) ( R ) = ( 3.75e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00616599 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584895 s | Solve Time: 0.253663 s + compositionalMultiphaseFlow: Max pressure change: 27682.798 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 855.107 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0029723224547379967 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-03 ) ( Rwell ) = ( 1.01e-09 ) ( R ) = ( 3.33e-03 ) + Last LinSolve(iter,res) = ( 3, 6.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00301962 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588641 s | Solve Time: 0.333426 s + compositionalMultiphaseFlow: Max pressure change: 1048.980 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.717 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.002978622186041391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-05 ) ( Rwell ) = ( 8.03e-13 ) ( R ) = ( 1.13e-05 ) + Last LinSolve(iter,res) = ( 4, 3.02e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13310343.07966251 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.306 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.64667e+06, 8.79904e+06, 9.84133e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.56732e+06, -1.51023e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.21986e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.3298e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.88688e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.21986e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.43102e+10 } } mol +Time: 6.71e+08 s, dt: 3497364.2689557006 s, Cycle: 170 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-01 ) ( Rwell ) = ( 4.97e-11 ) ( R ) = ( 4.82e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00453099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583596 s | Solve Time: 0.253634 s + compositionalMultiphaseFlow: Max pressure change: 29774.503 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 1021.839 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.004315236326468019 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-03 ) ( Rwell ) = ( 1.03e-09 ) ( R ) = ( 5.37e-03 ) + Last LinSolve(iter,res) = ( 3, 4.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00464225 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59011 s | Solve Time: 0.333223 s + compositionalMultiphaseFlow: Max pressure change: 1131.830 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.008 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.004314569726066919 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-05 ) ( Rwell ) = ( 1.70e-12 ) ( R ) = ( 2.24e-05 ) + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13335440.550682405 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.336 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.63766e+06, 8.80488e+06, 9.86456e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.57058e+06, -1.48726e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22158e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.33237e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.88835e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22158e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.60294e+10 } } mol +Time: 6.75e+08 s, dt: 4320000 s, Cycle: 171 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-01 ) ( Rwell ) = ( 2.63e-11 ) ( R ) = ( 3.51e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00379849 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586133 s | Solve Time: 0.253353 s + compositionalMultiphaseFlow: Max pressure change: 23453.099 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 828.990 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0028951875517899683 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-03 ) ( Rwell ) = ( 6.24e-10 ) ( R ) = ( 2.89e-03 ) + Last LinSolve(iter,res) = ( 3, 3.80e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.006991 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582788 s | Solve Time: 0.333335 s + compositionalMultiphaseFlow: Max pressure change: 774.694 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.407 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.002895411876888465 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-05 ) ( Rwell ) = ( 7.47e-13 ) ( R ) = ( 1.08e-05 ) + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13355148.498744953 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.264 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62963e+06, 8.81208e+06, 9.88281e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.57129e+06, -1.46403e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22371e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.33556e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89015e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22371e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.81531e+10 } } mol +Time: 6.79e+08 s, dt: 4320000 s, Cycle: 172 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.30e-01 ) ( Rwell ) = ( 1.64e-11 ) ( R ) = ( 2.30e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00283055 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585229 s | Solve Time: 0.253164 s + compositionalMultiphaseFlow: Max pressure change: 17541.478 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 630.344 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00168705737594943 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-03 ) ( Rwell ) = ( 3.42e-10 ) ( R ) = ( 1.69e-03 ) + Last LinSolve(iter,res) = ( 3, 2.83e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00936712 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582439 s | Solve Time: 0.332824 s + compositionalMultiphaseFlow: Max pressure change: 497.673 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 3.972 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0016882365646434527 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.19e-06 ) ( Rwell ) = ( 9.08e-15 ) ( R ) = ( 8.19e-06 ) + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13369857.414610963 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.194 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62435e+06, 8.81927e+06, 9.89643e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.56698e+06, -1.44578e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22583e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.33874e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89196e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22583e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 3.02767e+10 } } mol +Time: 6.84e+08 s, dt: 4320000 s, Cycle: 173 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-01 ) ( Rwell ) = ( 1.16e-11 ) ( R ) = ( 1.76e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00234864 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58721 s | Solve Time: 0.253479 s + compositionalMultiphaseFlow: Max pressure change: 14680.156 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 520.834 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0011492452943051568 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-03 ) ( Rwell ) = ( 2.26e-10 ) ( R ) = ( 1.15e-03 ) + Last LinSolve(iter,res) = ( 3, 2.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00221189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58305 s | Solve Time: 0.414341 s + compositionalMultiphaseFlow: Max pressure change: 359.475 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.472 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0011478359102579105 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-06 ) ( Rwell ) = ( 1.66e-13 ) ( R ) = ( 1.30e-06 ) + Last LinSolve(iter,res) = ( 5, 2.21e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13381882.279660195 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.162 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62134e+06, 8.82646e+06, 9.90757e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.55992e+06, -1.43216e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.22795e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.34193e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89376e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.22795e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 3.24003e+10 } } mol +Time: 6.88e+08 s, dt: 4320000 s, Cycle: 174 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-01 ) ( Rwell ) = ( 9.65e-12 ) ( R ) = ( 1.44e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00216617 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583732 s | Solve Time: 0.253782 s + compositionalMultiphaseFlow: Max pressure change: 12955.129 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 449.712 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0008468169902641209 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.47e-04 ) ( Rwell ) = ( 1.67e-10 ) ( R ) = ( 8.47e-04 ) + Last LinSolve(iter,res) = ( 3, 2.17e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13392539.542031493 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.001 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62022e+06, 8.83366e+06, 9.91744e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.55072e+06, -1.42102e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99998e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99998e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23008e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.34513e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89556e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23008e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 3.45235e+10 } } mol +Time: 6.92e+08 s, dt: 2142635.7310442924 s, Cycle: 175 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.25e-02 ) ( Rwell ) = ( 1.76e-10 ) ( R ) = ( 6.25e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00954913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582131 s | Solve Time: 0.174328 s + compositionalMultiphaseFlow: Max pressure change: 5846.281 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 207.955 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0006624332897740004 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-04 ) ( Rwell ) = ( 2.89e-11 ) ( R ) = ( 3.59e-04 ) + Last LinSolve(iter,res) = ( 2, 9.55e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13396962.144585637 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.065 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.001 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62007e+06, 8.83719e+06, 9.92154e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.54042e+06, -1.41115e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23113e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.3467e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89646e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23113e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 3.55752e+10 } } mol +Time: 6.94e+08 s, dt: 4285271.462088585 s, Cycle: 176 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-01 ) ( Rwell ) = ( 3.59e-11 ) ( R ) = ( 1.15e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0022958 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5817 s | Solve Time: 0.2532 s + compositionalMultiphaseFlow: Max pressure change: 11512.705 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 372.990 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00041595308462616387 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.81e-04 ) ( Rwell ) = ( 1.24e-10 ) ( R ) = ( 5.81e-04 ) + Last LinSolve(iter,res) = ( 3, 2.30e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13406156.72286991 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.129 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62102e+06, 8.84431e+06, 9.93006e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.53514e+06, -1.40705e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99998e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99998e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23324e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.34986e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.89825e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23324e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 3.76816e+10 } } mol +Time: 6.99e+08 s, dt: 4320000 s, Cycle: 177 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-01 ) ( Rwell ) = ( 1.31e-10 ) ( R ) = ( 1.05e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00258848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581064 s | Solve Time: 0.253709 s + compositionalMultiphaseFlow: Max pressure change: 10927.178 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 338.179 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.000197697230760574 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.74e-04 ) ( Rwell ) = ( 1.02e-10 ) ( R ) = ( 4.74e-04 ) + Last LinSolve(iter,res) = ( 3, 2.59e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13414528.884020241 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.121 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62295e+06, 8.85147e+06, 9.93782e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.52434e+06, -1.39853e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99998e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99998e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23536e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.35305e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90005e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23536e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 3.98047e+10 } } mol +Time: 7.03e+08 s, dt: 4320000 s, Cycle: 178 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-02 ) ( Rwell ) = ( 1.09e-10 ) ( R ) = ( 9.47e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00260956 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582843 s | Solve Time: 0.254617 s + compositionalMultiphaseFlow: Max pressure change: 10771.698 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 309.650 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0001363463439738588 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-04 ) ( Rwell ) = ( 9.43e-11 ) ( R ) = ( 4.02e-04 ) + Last LinSolve(iter,res) = ( 3, 2.61e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13422579.141546965 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62564e+06, 8.85863e+06, 9.94528e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.51347e+06, -1.39077e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99998e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99998e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23748e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.35623e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90186e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23748e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 4.1928e+10 } } mol +Time: 7.07e+08 s, dt: 4320000 s, Cycle: 179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.71e-02 ) ( Rwell ) = ( 1.01e-10 ) ( R ) = ( 8.71e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00264127 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581445 s | Solve Time: 0.253315 s + compositionalMultiphaseFlow: Max pressure change: 10555.421 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 288.288 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00011436202452175248 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-04 ) ( Rwell ) = ( 8.81e-11 ) ( R ) = ( 3.47e-04 ) + Last LinSolve(iter,res) = ( 3, 2.64e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13430369.238649223 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.62894e+06, 8.86579e+06, 9.9525e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.50274e+06, -1.38331e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99998e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99998e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.23961e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.35941e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90366e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.23961e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 4.40512e+10 } } mol +Time: 7.12e+08 s, dt: 4320000 s, Cycle: 180 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.00e-02 ) ( Rwell ) = ( 9.42e-11 ) ( R ) = ( 8.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00233076 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583585 s | Solve Time: 0.253205 s + compositionalMultiphaseFlow: Max pressure change: 10319.521 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 268.304 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.785765872532103e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.48e-04 ) ( Rwell ) = ( 8.35e-11 ) ( R ) = ( 7.48e-04 ) + Last LinSolve(iter,res) = ( 3, 2.33e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13437961.280569622 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.114 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.63273e+06, 8.87294e+06, 9.95954e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.49222e+06, -1.37609e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99998e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99998e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24173e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.3626e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90547e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24173e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 4.61746e+10 } } mol +Time: 7.16e+08 s, dt: 4320000 s, Cycle: 181 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.58e-02 ) ( Rwell ) = ( 8.94e-11 ) ( R ) = ( 7.58e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00211635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583477 s | Solve Time: 0.253476 s + compositionalMultiphaseFlow: Max pressure change: 10074.907 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 253.792 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.255991680465979e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.59e-04 ) ( Rwell ) = ( 8.01e-11 ) ( R ) = ( 9.59e-04 ) + Last LinSolve(iter,res) = ( 3, 2.12e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13445406.36662627 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.63691e+06, 8.88009e+06, 9.96644e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.48193e+06, -1.36906e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24385e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.36578e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90727e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24385e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 4.8298e+10 } } mol +Time: 7.20e+08 s, dt: 4320000 s, Cycle: 182 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.03e-02 ) ( Rwell ) = ( 8.59e-11 ) ( R ) = ( 7.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00217665 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582615 s | Solve Time: 0.253821 s + compositionalMultiphaseFlow: Max pressure change: 9837.459 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 236.105 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.9590910306495104e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-03 ) ( Rwell ) = ( 7.74e-11 ) ( R ) = ( 1.12e-03 ) + Last LinSolve(iter,res) = ( 3, 2.18e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00154218 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582563 s | Solve Time: 0.416536 s + compositionalMultiphaseFlow: Max pressure change: 99.619 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 2.901 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00023278896730904997 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.25e-07 ) ( Rwell ) = ( 1.13e-14 ) ( R ) = ( 4.25e-07 ) + Last LinSolve(iter,res) = ( 5, 1.54e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13452653.39712116 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.64144e+06, 8.88723e+06, 9.97315e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.47189e+06, -1.36215e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24598e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.36896e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90908e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24598e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 5.04216e+10 } } mol +Time: 7.25e+08 s, dt: 1354728.537911415 s, Cycle: 183 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-02 ) ( Rwell ) = ( 5.66e-12 ) ( R ) = ( 2.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0059064 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583824 s | Solve Time: 0.174295 s + compositionalMultiphaseFlow: Max pressure change: 3062.247 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 73.684 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2549515409808762e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.39e-05 ) ( Rwell ) = ( 7.76e-12 ) ( R ) = ( 7.39e-05 ) + Last LinSolve(iter,res) = ( 2, 5.91e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13454976.238765104 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.64289e+06, 8.88947e+06, 9.97531e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.46208e+06, -1.35544e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24664e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.36996e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.90965e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24664e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 5.10873e+10 } } mol +Time: 7.26e+08 s, dt: 2709457.07582283 s, Cycle: 184 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ( Rwell ) = ( 1.35e-11 ) ( R ) = ( 4.14e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00945393 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583213 s | Solve Time: 0.174382 s + compositionalMultiphaseFlow: Max pressure change: 6030.414 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 143.881 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.415231141088107e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.89e-04 ) ( Rwell ) = ( 3.03e-11 ) ( R ) = ( 3.89e-04 ) + Last LinSolve(iter,res) = ( 2, 9.45e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13459567.16671828 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.64589e+06, 8.89395e+06, 9.97956e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.45903e+06, -1.35328e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.24797e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.37196e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91078e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.24797e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 5.24189e+10 } } mol +Time: 7.29e+08 s, dt: 4320000 s, Cycle: 185 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.38e-02 ) ( Rwell ) = ( 3.60e-11 ) ( R ) = ( 6.38e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00268008 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585777 s | Solve Time: 0.253208 s + compositionalMultiphaseFlow: Max pressure change: 9440.888 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 214.923 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.00011180564635548951 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.86e-04 ) ( Rwell ) = ( 7.41e-11 ) ( R ) = ( 9.86e-04 ) + Last LinSolve(iter,res) = ( 3, 2.68e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13466755.591313958 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.104 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.65093e+06, 8.9011e+06, 9.98623e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.453e+06, -1.34903e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.2501e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.37515e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91258e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.2501e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 5.45424e+10 } } mol +Time: 7.33e+08 s, dt: 4320000 s, Cycle: 186 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-02 ) ( Rwell ) = ( 7.97e-11 ) ( R ) = ( 6.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00271236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582202 s | Solve Time: 0.253395 s + compositionalMultiphaseFlow: Max pressure change: 9243.436 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 207.065 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.135731007237631e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.71e-04 ) ( Rwell ) = ( 7.17e-11 ) ( R ) = ( 9.71e-04 ) + Last LinSolve(iter,res) = ( 3, 2.71e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13473836.898812855 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.101 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.65617e+06, 8.90824e+06, 9.99279e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.44362e+06, -1.34236e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.25222e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.37833e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91439e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.25222e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 5.66658e+10 } } mol +Time: 7.37e+08 s, dt: 4320000 s, Cycle: 187 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ( Rwell ) = ( 7.72e-11 ) ( R ) = ( 5.80e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00271894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583969 s | Solve Time: 0.2534 s + compositionalMultiphaseFlow: Max pressure change: 9075.795 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 198.137 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.46936134730802e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.42e-04 ) ( Rwell ) = ( 7.09e-11 ) ( R ) = ( 8.42e-04 ) + Last LinSolve(iter,res) = ( 3, 2.72e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13480884.061329667 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.099 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.6616e+06, 8.91538e+06, 9.99933e+06 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.43442e+06, -1.3358e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.25434e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.38152e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.91619e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.25434e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 5.87893e+10 } } mol +Time: 7.42e+08 s, dt: 4320000 s, Cycle: 188 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ( Rwell ) = ( 7.63e-11 ) ( R ) = ( 5.46e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00276088 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58327 s | Solve Time: 0.253401 s + compositionalMultiphaseFlow: Max pressure change: 8926.140 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 186.829 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.243556720788909e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.19e-04 ) ( Rwell ) = ( 6.99e-11 ) ( R ) = ( 8.19e-04 ) + Last LinSolve(iter,res) = ( 3, 2.76e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13487890.37093883 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.098 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.66718e+06, 8.92252e+06, 1.00058e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.42537e+06, -1.32926e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.25647e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.3847e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.918e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.25647e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 6.09127e+10 } } mol +Time: 7.46e+08 s, dt: 4320000 s, Cycle: 189 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ( Rwell ) = ( 7.53e-11 ) ( R ) = ( 5.23e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00312591 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582856 s | Solve Time: 0.253484 s + compositionalMultiphaseFlow: Max pressure change: 8793.608 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 181.249 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7923824124753693e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.74e-04 ) ( Rwell ) = ( 6.90e-11 ) ( R ) = ( 8.74e-04 ) + Last LinSolve(iter,res) = ( 3, 3.13e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13494859.861846719 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.096 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.67289e+06, 8.92965e+06, 1.00123e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.41648e+06, -1.32276e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.25859e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.38789e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9198e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.25859e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 6.30359e+10 } } mol +Time: 7.50e+08 s, dt: 4320000 s, Cycle: 190 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ( Rwell ) = ( 7.44e-11 ) ( R ) = ( 5.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00316207 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.580661 s | Solve Time: 0.253174 s + compositionalMultiphaseFlow: Max pressure change: 8673.119 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 174.619 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4240811002718132e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.39e-04 ) ( Rwell ) = ( 6.81e-11 ) ( R ) = ( 7.39e-04 ) + Last LinSolve(iter,res) = ( 3, 3.16e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13501794.358467828 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.095 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.67872e+06, 8.93678e+06, 1.00187e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.40772e+06, -1.3163e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26071e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.39107e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92161e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26071e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 6.51591e+10 } } mol +Time: 7.55e+08 s, dt: 2930542.92417717 s, Cycle: 191 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.26e-02 ) ( Rwell ) = ( 7.35e-11 ) ( R ) = ( 3.26e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0027947 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583023 s | Solve Time: 0.253537 s + compositionalMultiphaseFlow: Max pressure change: 5833.397 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 114.751 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.225707518543345e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-04 ) ( Rwell ) = ( 3.05e-11 ) ( R ) = ( 3.78e-04 ) + Last LinSolve(iter,res) = ( 3, 2.79e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13506443.634879617 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.064 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.68272e+06, 8.94161e+06, 1.0023e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.39908e+06, -1.30987e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26215e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.39323e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92283e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26215e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 6.65995e+10 } } mol +Time: 7.57e+08 s, dt: 4320000 s, Cycle: 192 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ( Rwell ) = ( 3.58e-11 ) ( R ) = ( 4.66e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00320414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582037 s | Solve Time: 0.253377 s + compositionalMultiphaseFlow: Max pressure change: 8504.175 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 162.532 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.8303124348846325e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.39e-04 ) ( Rwell ) = ( 6.79e-11 ) ( R ) = ( 6.39e-04 ) + Last LinSolve(iter,res) = ( 3, 3.20e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13513377.481744515 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.094 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.68872e+06, 8.94874e+06, 1.00295e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.39327e+06, -1.30556e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26428e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.39642e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92463e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26428e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 6.87227e+10 } } mol +Time: 7.62e+08 s, dt: 4320000 s, Cycle: 193 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ( Rwell ) = ( 7.32e-11 ) ( R ) = ( 4.55e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00325541 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583281 s | Solve Time: 0.253236 s + compositionalMultiphaseFlow: Max pressure change: 8419.526 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 158.518 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7648310067674977e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.82e-04 ) ( Rwell ) = ( 6.62e-11 ) ( R ) = ( 5.82e-04 ) + Last LinSolve(iter,res) = ( 3, 3.26e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13520236.44758728 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.6948e+06, 8.95587e+06, 1.00358e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.3848e+06, -1.29913e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.2664e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.3996e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92644e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.2664e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 7.08459e+10 } } mol +Time: 7.66e+08 s, dt: 4320000 s, Cycle: 194 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ( Rwell ) = ( 7.15e-11 ) ( R ) = ( 4.38e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00346359 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58602 s | Solve Time: 0.25412 s + compositionalMultiphaseFlow: Max pressure change: 8347.981 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 152.614 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5437908547966117e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.22e-04 ) ( Rwell ) = ( 6.58e-11 ) ( R ) = ( 6.22e-04 ) + Last LinSolve(iter,res) = ( 3, 3.46e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13527077.990568765 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.70095e+06, 8.96299e+06, 1.00422e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.37641e+06, -1.29276e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.26852e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.40279e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.92824e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.26852e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 7.29691e+10 } } mol +Time: 7.70e+08 s, dt: 4320000 s, Cycle: 195 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ( Rwell ) = ( 7.10e-11 ) ( R ) = ( 4.24e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00337144 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584455 s | Solve Time: 0.253687 s + compositionalMultiphaseFlow: Max pressure change: 8294.096 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 149.129 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.36433365609534e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.26e-04 ) ( Rwell ) = ( 6.53e-11 ) ( R ) = ( 7.26e-04 ) + Last LinSolve(iter,res) = ( 3, 3.37e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13533902.011151426 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.70716e+06, 8.97011e+06, 1.00485e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.3681e+06, -1.28642e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27064e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.40597e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93005e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27064e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 7.50923e+10 } } mol +Time: 7.75e+08 s, dt: 4320000 s, Cycle: 196 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ( Rwell ) = ( 7.05e-11 ) ( R ) = ( 4.11e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00326081 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587293 s | Solve Time: 0.253689 s + compositionalMultiphaseFlow: Max pressure change: 8256.602 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 144.378 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4100197058719566e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-04 ) ( Rwell ) = ( 6.48e-11 ) ( R ) = ( 5.59e-04 ) + Last LinSolve(iter,res) = ( 3, 3.26e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13540710.066454664 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.71343e+06, 8.97723e+06, 1.00548e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.35985e+06, -1.28009e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27277e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.40916e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93185e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27277e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 7.72156e+10 } } mol +Time: 7.79e+08 s, dt: 4320000 s, Cycle: 197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-02 ) ( Rwell ) = ( 7.00e-11 ) ( R ) = ( 3.95e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00293237 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582752 s | Solve Time: 0.252885 s + compositionalMultiphaseFlow: Max pressure change: 8222.773 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 139.876 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1594090021826986e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.78e-04 ) ( Rwell ) = ( 6.44e-11 ) ( R ) = ( 6.78e-04 ) + Last LinSolve(iter,res) = ( 3, 2.93e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13547502.387851056 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.090 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.71975e+06, 8.98435e+06, 1.00611e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.35166e+06, -1.27377e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27489e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.41234e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93366e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27489e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 7.9339e+10 } } mol +Time: 7.83e+08 s, dt: 4320000 s, Cycle: 198 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ( Rwell ) = ( 6.96e-11 ) ( R ) = ( 3.90e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00352845 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582093 s | Solve Time: 0.263898 s + compositionalMultiphaseFlow: Max pressure change: 8191.998 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 137.871 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1655816547384568e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-04 ) ( Rwell ) = ( 6.40e-11 ) ( R ) = ( 5.48e-04 ) + Last LinSolve(iter,res) = ( 3, 3.53e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13554284.602874475 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.090 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.72611e+06, 8.99147e+06, 1.00674e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.34352e+06, -1.26747e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27701e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.41552e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93546e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27701e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 8.14621e+10 } } mol +Time: 7.88e+08 s, dt: 1320000 s, Cycle: 199 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ( Rwell ) = ( 6.92e-11 ) ( R ) = ( 1.16e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00723113 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585553 s | Solve Time: 0.174652 s + compositionalMultiphaseFlow: Max pressure change: 2474.878 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.034 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.160736554945313e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.83e-05 ) ( Rwell ) = ( 5.74e-12 ) ( R ) = ( 5.83e-05 ) + Last LinSolve(iter,res) = ( 2, 7.23e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13556312.192903653 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.72805e+06, 8.99363e+06, 1.00693e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.33544e+06, -1.26117e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27766e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.41649e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93601e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27766e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 8.21103e+10 } } mol +Time: 7.89e+08 s, dt: 2640000 s, Cycle: 200 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.29e-02 ) ( Rwell ) = ( 1.08e-11 ) ( R ) = ( 2.29e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00263431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583949 s | Solve Time: 0.253447 s + compositionalMultiphaseFlow: Max pressure change: 5009.890 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 82.551 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1309485749965162e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-04 ) ( Rwell ) = ( 2.39e-11 ) ( R ) = ( 1.02e-04 ) + Last LinSolve(iter,res) = ( 3, 2.63e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13560462.694758248 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.73196e+06, 8.99798e+06, 1.00731e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.33298e+06, -1.25929e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.27896e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.41844e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93712e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.27896e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 8.34079e+10 } } mol +Time: 7.92e+08 s, dt: 4320000 s, Cycle: 201 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-02 ) ( Rwell ) = ( 2.91e-11 ) ( R ) = ( 3.68e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368895 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583827 s | Solve Time: 0.253148 s + compositionalMultiphaseFlow: Max pressure change: 8160.588 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 130.584 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.450105387399095e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.79e-04 ) ( Rwell ) = ( 6.39e-11 ) ( R ) = ( 5.79e-04 ) + Last LinSolve(iter,res) = ( 3, 3.69e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13567252.043323994 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.089 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.73839e+06, 9.00509e+06, 1.00795e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.32806e+06, -1.25544e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28108e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.42163e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.93892e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28108e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 8.55311e+10 } } mol +Time: 7.96e+08 s, dt: 4320000 s, Cycle: 202 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-02 ) ( Rwell ) = ( 6.91e-11 ) ( R ) = ( 3.57e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00328571 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5837 s | Solve Time: 0.252904 s + compositionalMultiphaseFlow: Max pressure change: 8114.136 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 127.721 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.146422764616524e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-04 ) ( Rwell ) = ( 6.29e-11 ) ( R ) = ( 4.34e-04 ) + Last LinSolve(iter,res) = ( 3, 3.29e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13573996.89666762 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.089 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.74485e+06, 9.0122e+06, 1.00857e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.32004e+06, -1.24914e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28321e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.42481e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94072e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28321e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 8.76545e+10 } } mol +Time: 8.00e+08 s, dt: 4320000 s, Cycle: 203 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ( Rwell ) = ( 6.81e-11 ) ( R ) = ( 3.52e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00332874 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58381 s | Solve Time: 0.252687 s + compositionalMultiphaseFlow: Max pressure change: 8093.218 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 125.452 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.674788237044261e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-04 ) ( Rwell ) = ( 6.27e-11 ) ( R ) = ( 5.58e-04 ) + Last LinSolve(iter,res) = ( 3, 3.33e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13580737.87959567 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.75133e+06, 9.01931e+06, 1.0092e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.31206e+06, -1.24288e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28533e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.428e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94253e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28533e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 8.97778e+10 } } mol +Time: 8.05e+08 s, dt: 4320000 s, Cycle: 204 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-02 ) ( Rwell ) = ( 6.78e-11 ) ( R ) = ( 3.44e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00315211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584232 s | Solve Time: 0.253064 s + compositionalMultiphaseFlow: Max pressure change: 8071.694 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 122.775 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.310224978906987e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-04 ) ( Rwell ) = ( 6.24e-11 ) ( R ) = ( 4.54e-04 ) + Last LinSolve(iter,res) = ( 3, 3.15e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13587470.814185495 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.75784e+06, 9.02642e+06, 1.00982e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.30411e+06, -1.23662e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28745e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.43118e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94433e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28745e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 9.19012e+10 } } mol +Time: 8.09e+08 s, dt: 4320000 s, Cycle: 205 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.33e-02 ) ( Rwell ) = ( 6.75e-11 ) ( R ) = ( 3.33e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00350708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58744 s | Solve Time: 0.253633 s + compositionalMultiphaseFlow: Max pressure change: 8051.863 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 119.265 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.891931532249096e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-04 ) ( Rwell ) = ( 6.22e-11 ) ( R ) = ( 4.95e-04 ) + Last LinSolve(iter,res) = ( 3, 3.51e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13594198.64442867 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.76436e+06, 9.03352e+06, 1.01045e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.29617e+06, -1.23037e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.28958e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.43437e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94614e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.28958e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 9.40246e+10 } } mol +Time: 8.13e+08 s, dt: 4320000 s, Cycle: 206 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-02 ) ( Rwell ) = ( 6.73e-11 ) ( R ) = ( 3.24e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00348228 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582167 s | Solve Time: 0.253364 s + compositionalMultiphaseFlow: Max pressure change: 8031.783 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 115.942 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.2392670474586964e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e-04 ) ( Rwell ) = ( 6.19e-11 ) ( R ) = ( 4.46e-04 ) + Last LinSolve(iter,res) = ( 3, 3.48e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13600919.202899225 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.7709e+06, 9.04062e+06, 1.01107e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.28827e+06, -1.22413e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.2917e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.43755e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.94794e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.2917e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 9.6148e+10 } } mol +Time: 8.18e+08 s, dt: 3000000 s, Cycle: 207 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-02 ) ( Rwell ) = ( 6.70e-11 ) ( R ) = ( 2.22e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00295779 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58229 s | Solve Time: 0.253965 s + compositionalMultiphaseFlow: Max pressure change: 5550.523 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 80.067 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.070602573485015e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-04 ) ( Rwell ) = ( 2.95e-11 ) ( R ) = ( 1.33e-04 ) + Last LinSolve(iter,res) = ( 3, 2.96e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13605563.371812414 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.060 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.77545e+06, 9.04555e+06, 1.0115e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.28038e+06, -1.21789e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.29317e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.43976e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9492e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.29317e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 9.76225e+10 } } mol +Time: 8.21e+08 s, dt: 4320000 s, Cycle: 208 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.15e-02 ) ( Rwell ) = ( 3.46e-11 ) ( R ) = ( 3.15e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00352522 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582963 s | Solve Time: 0.252946 s + compositionalMultiphaseFlow: Max pressure change: 8019.119 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 113.398 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.764588498338494e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.93e-04 ) ( Rwell ) = ( 6.19e-11 ) ( R ) = ( 4.93e-04 ) + Last LinSolve(iter,res) = ( 3, 3.53e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13612295.095146533 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.78201e+06, 9.05265e+06, 1.01213e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.27491e+06, -1.21358e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.2953e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.44295e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.951e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.2953e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 9.97459e+10 } } mol +Time: 8.25e+08 s, dt: 4320000 s, Cycle: 209 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.08e-02 ) ( Rwell ) = ( 6.70e-11 ) ( R ) = ( 3.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00355002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581947 s | Solve Time: 0.252618 s + compositionalMultiphaseFlow: Max pressure change: 7984.299 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 110.916 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.898847746821367e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.28e-04 ) ( Rwell ) = ( 6.12e-11 ) ( R ) = ( 4.28e-04 ) + Last LinSolve(iter,res) = ( 3, 3.55e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13618999.768224483 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.78858e+06, 9.05974e+06, 1.01275e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.26706e+06, -1.20733e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.29742e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.44613e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95281e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.29742e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.01869e+11 } } mol +Time: 8.29e+08 s, dt: 4320000 s, Cycle: 210 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.99e-02 ) ( Rwell ) = ( 6.63e-11 ) ( R ) = ( 2.99e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00414949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587615 s | Solve Time: 0.252796 s + compositionalMultiphaseFlow: Max pressure change: 7975.338 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 107.984 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.657121877056248e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.45e-04 ) ( Rwell ) = ( 6.10e-11 ) ( R ) = ( 4.45e-04 ) + Last LinSolve(iter,res) = ( 3, 4.15e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13625700.245451998 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.79516e+06, 9.06683e+06, 1.01337e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.25921e+06, -1.2011e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.29954e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.44932e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95461e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.29954e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.03992e+11 } } mol +Time: 8.34e+08 s, dt: 4320000 s, Cycle: 211 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.95e-02 ) ( Rwell ) = ( 6.61e-11 ) ( R ) = ( 2.95e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00421402 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582962 s | Solve Time: 0.253514 s + compositionalMultiphaseFlow: Max pressure change: 7968.229 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 106.818 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.3386817208123105e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-04 ) ( Rwell ) = ( 6.08e-11 ) ( R ) = ( 4.54e-04 ) + Last LinSolve(iter,res) = ( 3, 4.21e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13632396.593023956 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.80175e+06, 9.07393e+06, 1.01399e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.25138e+06, -1.19488e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30167e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.4525e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95642e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30167e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.06115e+11 } } mol +Time: 8.38e+08 s, dt: 4320000 s, Cycle: 212 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.90e-02 ) ( Rwell ) = ( 6.59e-11 ) ( R ) = ( 2.90e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00424892 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583648 s | Solve Time: 0.25276 s + compositionalMultiphaseFlow: Max pressure change: 7960.984 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 105.038 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.5527780189468245e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-04 ) ( Rwell ) = ( 6.06e-11 ) ( R ) = ( 4.02e-04 ) + Last LinSolve(iter,res) = ( 3, 4.25e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13639089.06920784 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.80835e+06, 9.08101e+06, 1.01461e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.24357e+06, -1.18866e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30379e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.45569e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.95822e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30379e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.08238e+11 } } mol +Time: 8.42e+08 s, dt: 4320000 s, Cycle: 213 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.82e-02 ) ( Rwell ) = ( 6.57e-11 ) ( R ) = ( 2.82e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00456819 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584029 s | Solve Time: 0.252908 s + compositionalMultiphaseFlow: Max pressure change: 7953.595 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 102.719 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.510343149550678e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-04 ) ( Rwell ) = ( 6.04e-11 ) ( R ) = ( 3.86e-04 ) + Last LinSolve(iter,res) = ( 3, 4.57e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13645777.53362764 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.81495e+06, 9.0881e+06, 1.01524e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.23576e+06, -1.18245e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30591e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.45887e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96002e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30591e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.10362e+11 } } mol +Time: 8.46e+08 s, dt: 4320000 s, Cycle: 214 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.79e-02 ) ( Rwell ) = ( 6.54e-11 ) ( R ) = ( 2.79e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00408401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586183 s | Solve Time: 0.253576 s + compositionalMultiphaseFlow: Max pressure change: 7946.548 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 101.282 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.13014589409444e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-04 ) ( Rwell ) = ( 6.02e-11 ) ( R ) = ( 4.05e-04 ) + Last LinSolve(iter,res) = ( 3, 4.08e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13652462.026988462 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.82156e+06, 9.09518e+06, 1.01586e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.22796e+06, -1.17623e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30803e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.46205e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96183e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30803e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.12485e+11 } } mol +Time: 8.51e+08 s, dt: 1320000 s, Cycle: 215 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.43e-03 ) ( Rwell ) = ( 6.52e-11 ) ( R ) = ( 8.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00845987 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583605 s | Solve Time: 0.174318 s + compositionalMultiphaseFlow: Max pressure change: 2398.045 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 30.974 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.948261288122534e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-05 ) ( Rwell ) = ( 5.54e-12 ) ( R ) = ( 5.76e-05 ) + Last LinSolve(iter,res) = ( 2, 8.46e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13654486.761778597 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.82358e+06, 9.09734e+06, 1.01604e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.22016e+06, -1.17002e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30868e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.46302e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96238e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30868e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.13133e+11 } } mol +Time: 8.52e+08 s, dt: 2640000 s, Cycle: 216 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-02 ) ( Rwell ) = ( 1.05e-11 ) ( R ) = ( 1.68e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00288333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585911 s | Solve Time: 0.253083 s + compositionalMultiphaseFlow: Max pressure change: 4866.683 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 61.498 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1765762211513042e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 2.24e-11 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 3, 2.88e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13658569.391793942 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.053 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.82762e+06, 9.10167e+06, 1.01642e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.21778e+06, -1.16814e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.30998e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.46497e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96348e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.30998e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.1443e+11 } } mol +Time: 8.55e+08 s, dt: 4320000 s, Cycle: 217 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-02 ) ( Rwell ) = ( 2.74e-11 ) ( R ) = ( 2.72e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00361817 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581863 s | Solve Time: 0.253252 s + compositionalMultiphaseFlow: Max pressure change: 7948.746 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 99.262 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.555943438065089e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.93e-04 ) ( Rwell ) = ( 6.02e-11 ) ( R ) = ( 3.93e-04 ) + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13665267.38625807 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.83425e+06, 9.10876e+06, 1.01705e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.21303e+06, -1.16435e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3121e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.46816e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96529e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3121e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.16554e+11 } } mol +Time: 8.59e+08 s, dt: 4320000 s, Cycle: 218 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.66e-02 ) ( Rwell ) = ( 6.52e-11 ) ( R ) = ( 2.66e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00394821 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582919 s | Solve Time: 0.252767 s + compositionalMultiphaseFlow: Max pressure change: 7925.835 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 97.486 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.793576268036226e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-04 ) ( Rwell ) = ( 5.97e-11 ) ( R ) = ( 3.54e-04 ) + Last LinSolve(iter,res) = ( 3, 3.95e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13671944.920005333 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.84087e+06, 9.11584e+06, 1.01767e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.20525e+06, -1.15813e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.31423e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.47134e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.96709e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.31423e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.18677e+11 } } mol +Time: 8.63e+08 s, dt: 4320000 s, Cycle: 219 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.60e-02 ) ( Rwell ) = ( 6.47e-11 ) ( R ) = ( 2.60e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368747 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588307 s | Solve Time: 0.253047 s + compositionalMultiphaseFlow: Max pressure change: 7921.367 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 95.324 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.447659377015967e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-04 ) ( Rwell ) = ( 5.95e-11 ) ( R ) = ( 2.04e-04 ) + Last LinSolve(iter,res) = ( 3, 3.69e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13678619.699985627 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.84749e+06, 9.12292e+06, 1.01829e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.19748e+06, -1.15193e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.31635e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.47453e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9689e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.31635e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.20801e+11 } } mol +Time: 8.68e+08 s, dt: 4320000 s, Cycle: 220 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.57e-02 ) ( Rwell ) = ( 6.45e-11 ) ( R ) = ( 2.57e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00372939 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588879 s | Solve Time: 0.252995 s + compositionalMultiphaseFlow: Max pressure change: 7913.547 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 93.978 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.759759249377659e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-04 ) ( Rwell ) = ( 5.93e-11 ) ( R ) = ( 3.34e-04 ) + Last LinSolve(iter,res) = ( 3, 3.73e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13685293.17108159 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.85412e+06, 9.12999e+06, 1.01891e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.18971e+06, -1.14573e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.31847e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.47771e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9707e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.31847e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.22924e+11 } } mol +Time: 8.72e+08 s, dt: 4320000 s, Cycle: 221 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-02 ) ( Rwell ) = ( 6.44e-11 ) ( R ) = ( 2.54e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00352598 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583667 s | Solve Time: 0.252644 s + compositionalMultiphaseFlow: Max pressure change: 7905.968 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 93.221 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.284097008005027e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-04 ) ( Rwell ) = ( 5.92e-11 ) ( R ) = ( 3.38e-04 ) + Last LinSolve(iter,res) = ( 3, 3.53e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13691963.808112713 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.86075e+06, 9.13707e+06, 1.01953e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.18195e+06, -1.13952e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3206e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.4809e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97251e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3206e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.25047e+11 } } mol +Time: 8.76e+08 s, dt: 4320000 s, Cycle: 222 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-02 ) ( Rwell ) = ( 6.42e-11 ) ( R ) = ( 2.50e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00364961 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585828 s | Solve Time: 0.252345 s + compositionalMultiphaseFlow: Max pressure change: 7896.082 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 92.085 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.067706068866528e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-04 ) ( Rwell ) = ( 5.90e-11 ) ( R ) = ( 3.94e-04 ) + Last LinSolve(iter,res) = ( 3, 3.65e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13698631.838363413 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.86738e+06, 9.14414e+06, 1.02015e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.17419e+06, -1.13333e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.32272e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.48408e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97431e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.32272e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.2717e+11 } } mol +Time: 8.81e+08 s, dt: 3000000 s, Cycle: 223 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-02 ) ( Rwell ) = ( 6.40e-11 ) ( R ) = ( 1.70e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00352761 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584391 s | Solve Time: 0.253066 s + compositionalMultiphaseFlow: Max pressure change: 5469.255 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 63.290 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8682485299459373e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 2.82e-11 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 3, 3.53e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13703250.403361417 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.87198e+06, 9.14905e+06, 1.02058e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.16643e+06, -1.12713e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.32419e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.48629e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97556e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.32419e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.28645e+11 } } mol +Time: 8.84e+08 s, dt: 4320000 s, Cycle: 224 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-02 ) ( Rwell ) = ( 3.32e-11 ) ( R ) = ( 2.41e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00322199 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586939 s | Solve Time: 0.252527 s + compositionalMultiphaseFlow: Max pressure change: 7897.871 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 89.341 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7038685880543802e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-04 ) ( Rwell ) = ( 5.90e-11 ) ( R ) = ( 2.94e-04 ) + Last LinSolve(iter,res) = ( 3, 3.22e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13709927.977169015 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.87862e+06, 9.15612e+06, 1.0212e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.16105e+06, -1.12284e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.32632e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.48948e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97737e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.32632e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.30768e+11 } } mol +Time: 8.88e+08 s, dt: 4320000 s, Cycle: 225 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.37e-02 ) ( Rwell ) = ( 6.40e-11 ) ( R ) = ( 2.37e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00282445 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583242 s | Solve Time: 0.252997 s + compositionalMultiphaseFlow: Max pressure change: 7886.746 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 87.453 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.683023832801169e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e-04 ) ( Rwell ) = ( 5.85e-11 ) ( R ) = ( 3.03e-04 ) + Last LinSolve(iter,res) = ( 3, 2.82e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13716590.412734633 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.88525e+06, 9.16319e+06, 1.02181e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.15331e+06, -1.11663e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.32844e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.49266e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.97917e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.32844e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.32892e+11 } } mol +Time: 8.92e+08 s, dt: 4320000 s, Cycle: 226 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.35e-02 ) ( Rwell ) = ( 6.35e-11 ) ( R ) = ( 2.35e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368035 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585413 s | Solve Time: 0.252585 s + compositionalMultiphaseFlow: Max pressure change: 7886.077 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 86.840 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.1925381496211713e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.11e-04 ) ( Rwell ) = ( 5.84e-11 ) ( R ) = ( 3.11e-04 ) + Last LinSolve(iter,res) = ( 3, 3.68e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13723253.648443058 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.89188e+06, 9.17025e+06, 1.02243e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.14556e+06, -1.11044e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33056e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.49585e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98098e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33056e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.35015e+11 } } mol +Time: 8.97e+08 s, dt: 4320000 s, Cycle: 227 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.32e-02 ) ( Rwell ) = ( 6.34e-11 ) ( R ) = ( 2.32e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00320174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584122 s | Solve Time: 0.256084 s + compositionalMultiphaseFlow: Max pressure change: 7883.273 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 86.013 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2442326955983702e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-04 ) ( Rwell ) = ( 5.82e-11 ) ( R ) = ( 3.25e-04 ) + Last LinSolve(iter,res) = ( 3, 3.20e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13729912.389607923 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.89851e+06, 9.17732e+06, 1.02305e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.13782e+06, -1.10425e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33269e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.49903e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98278e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33269e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.37138e+11 } } mol +Time: 9.01e+08 s, dt: 4320000 s, Cycle: 228 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.28e-02 ) ( Rwell ) = ( 6.32e-11 ) ( R ) = ( 2.28e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00341296 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585767 s | Solve Time: 0.252954 s + compositionalMultiphaseFlow: Max pressure change: 7881.267 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 84.908 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.596435866641933e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.92e-04 ) ( Rwell ) = ( 5.81e-11 ) ( R ) = ( 2.92e-04 ) + Last LinSolve(iter,res) = ( 3, 3.41e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13736570.84695277 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.90515e+06, 9.18438e+06, 1.02367e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.13008e+06, -1.09806e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33481e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.50222e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98459e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33481e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.39261e+11 } } mol +Time: 9.05e+08 s, dt: 4320000 s, Cycle: 229 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.24e-02 ) ( Rwell ) = ( 6.31e-11 ) ( R ) = ( 2.24e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00300255 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585615 s | Solve Time: 0.252964 s + compositionalMultiphaseFlow: Max pressure change: 7878.913 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 83.493 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.732448870612636e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-04 ) ( Rwell ) = ( 5.79e-11 ) ( R ) = ( 2.97e-04 ) + Last LinSolve(iter,res) = ( 3, 3.00e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13743226.121860651 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.91178e+06, 9.19144e+06, 1.02429e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.12235e+06, -1.09187e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33693e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5054e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98639e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33693e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.41385e+11 } } mol +Time: 9.10e+08 s, dt: 4320000 s, Cycle: 230 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.23e-02 ) ( Rwell ) = ( 6.29e-11 ) ( R ) = ( 2.23e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00376223 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589894 s | Solve Time: 0.252532 s + compositionalMultiphaseFlow: Max pressure change: 7878.243 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 82.762 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.792684433150505e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-04 ) ( Rwell ) = ( 5.78e-11 ) ( R ) = ( 2.99e-04 ) + Last LinSolve(iter,res) = ( 3, 3.76e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13749881.805124935 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.91841e+06, 9.1985e+06, 1.02491e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.11461e+06, -1.08568e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.33906e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.50859e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.9882e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.33906e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.43508e+11 } } mol +Time: 9.14e+08 s, dt: 1320000 s, Cycle: 231 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.75e-03 ) ( Rwell ) = ( 6.27e-11 ) ( R ) = ( 6.75e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00891803 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584234 s | Solve Time: 0.173949 s + compositionalMultiphaseFlow: Max pressure change: 2383.399 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25.297 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6000378209656283e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-05 ) ( Rwell ) = ( 5.37e-12 ) ( R ) = ( 5.40e-05 ) + Last LinSolve(iter,res) = ( 2, 8.92e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13751906.373825235 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.92044e+06, 9.20065e+06, 1.0251e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.10688e+06, -1.07949e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.3397e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.50956e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98875e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.3397e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.44156e+11 } } mol +Time: 9.15e+08 s, dt: 2640000 s, Cycle: 232 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ( Rwell ) = ( 1.03e-11 ) ( R ) = ( 1.34e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00311637 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58684 s | Solve Time: 0.252817 s + compositionalMultiphaseFlow: Max pressure change: 4820.954 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.361 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.89155740044123e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.45e-05 ) ( Rwell ) = ( 2.14e-11 ) ( R ) = ( 9.45e-05 ) + Last LinSolve(iter,res) = ( 3, 3.12e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13755964.031675695 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.92449e+06, 9.20496e+06, 1.02548e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.10452e+06, -1.07761e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.341e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5115e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.98985e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.341e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.45454e+11 } } mol +Time: 9.18e+08 s, dt: 4320000 s, Cycle: 233 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-02 ) ( Rwell ) = ( 2.64e-11 ) ( R ) = ( 2.19e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00339025 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585032 s | Solve Time: 0.253972 s + compositionalMultiphaseFlow: Max pressure change: 7882.688 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 81.642 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.733369755263503e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-04 ) ( Rwell ) = ( 5.77e-11 ) ( R ) = ( 2.57e-04 ) + Last LinSolve(iter,res) = ( 3, 3.39e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13762625.985966804 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.93112e+06, 9.21202e+06, 1.02609e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.0998e+06, -1.07384e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.34313e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.51469e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99166e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.34313e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.47577e+11 } } mol +Time: 9.22e+08 s, dt: 4320000 s, Cycle: 234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-02 ) ( Rwell ) = ( 6.26e-11 ) ( R ) = ( 2.15e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0032237 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584641 s | Solve Time: 0.253193 s + compositionalMultiphaseFlow: Max pressure change: 7867.114 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 80.642 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2286295215945273e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-04 ) ( Rwell ) = ( 5.73e-11 ) ( R ) = ( 2.54e-04 ) + Last LinSolve(iter,res) = ( 3, 3.22e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13769275.064065404 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.93775e+06, 9.21907e+06, 1.02671e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.09207e+06, -1.06765e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.34525e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.51787e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99346e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.34525e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.497e+11 } } mol +Time: 9.27e+08 s, dt: 4320000 s, Cycle: 235 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-02 ) ( Rwell ) = ( 6.22e-11 ) ( R ) = ( 2.11e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00311261 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585027 s | Solve Time: 0.25268 s + compositionalMultiphaseFlow: Max pressure change: 7863.947 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 79.410 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.632615973663377e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-04 ) ( Rwell ) = ( 5.72e-11 ) ( R ) = ( 2.97e-04 ) + Last LinSolve(iter,res) = ( 3, 3.11e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13775922.461379085 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.94439e+06, 9.22612e+06, 1.02733e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.08435e+06, -1.06146e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.34737e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.52106e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99527e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.34737e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.51824e+11 } } mol +Time: 9.31e+08 s, dt: 4320000 s, Cycle: 236 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-02 ) ( Rwell ) = ( 6.21e-11 ) ( R ) = ( 2.10e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00345395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586253 s | Solve Time: 0.252889 s + compositionalMultiphaseFlow: Max pressure change: 7860.338 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 78.496 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.226499106194879e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-04 ) ( Rwell ) = ( 5.70e-11 ) ( R ) = ( 2.54e-04 ) + Last LinSolve(iter,res) = ( 3, 3.45e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13782568.058355805 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.95101e+06, 9.23317e+06, 1.02795e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.07663e+06, -1.05528e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.34949e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.52424e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99707e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.34949e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.53947e+11 } } mol +Time: 9.35e+08 s, dt: 4320000 s, Cycle: 237 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-02 ) ( Rwell ) = ( 6.19e-11 ) ( R ) = ( 2.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00347611 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587257 s | Solve Time: 0.253143 s + compositionalMultiphaseFlow: Max pressure change: 7855.607 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 78.136 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0356396508436347e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-04 ) ( Rwell ) = ( 5.69e-11 ) ( R ) = ( 2.55e-04 ) + Last LinSolve(iter,res) = ( 3, 3.48e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13789212.354834335 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.95764e+06, 9.24022e+06, 1.02857e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.06891e+06, -1.0491e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35162e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.52743e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 1.99888e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35162e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.5607e+11 } } mol +Time: 9.39e+08 s, dt: 4320000 s, Cycle: 238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.06e-02 ) ( Rwell ) = ( 6.18e-11 ) ( R ) = ( 2.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00347483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587725 s | Solve Time: 0.253369 s + compositionalMultiphaseFlow: Max pressure change: 7850.113 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 77.536 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.09770432202383e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-04 ) ( Rwell ) = ( 5.67e-11 ) ( R ) = ( 2.01e-04 ) + Last LinSolve(iter,res) = ( 3, 3.47e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13795855.050278699 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.96427e+06, 9.24726e+06, 1.02918e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.06119e+06, -1.04292e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35374e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.53061e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00068e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35374e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.58193e+11 } } mol +Time: 9.44e+08 s, dt: 3000000 s, Cycle: 239 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-02 ) ( Rwell ) = ( 6.16e-11 ) ( R ) = ( 1.41e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00323953 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586845 s | Solve Time: 0.253145 s + compositionalMultiphaseFlow: Max pressure change: 5439.298 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.490 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3110884860334515e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-04 ) ( Rwell ) = ( 2.72e-11 ) ( R ) = ( 1.04e-04 ) + Last LinSolve(iter,res) = ( 3, 3.24e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13800458.169447675 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.058 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.96887e+06, 9.25215e+06, 1.02961e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.05347e+06, -1.03674e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35522e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.53282e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00193e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35522e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.59668e+11 } } mol +Time: 9.47e+08 s, dt: 4320000 s, Cycle: 240 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.01e-02 ) ( Rwell ) = ( 3.21e-11 ) ( R ) = ( 2.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00338587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586512 s | Solve Time: 0.253175 s + compositionalMultiphaseFlow: Max pressure change: 7852.302 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 76.018 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2390070073031723e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-04 ) ( Rwell ) = ( 5.66e-11 ) ( R ) = ( 2.39e-04 ) + Last LinSolve(iter,res) = ( 3, 3.39e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13807106.389954459 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.97549e+06, 9.2592e+06, 1.03023e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.04812e+06, -1.03246e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35734e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.53601e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00374e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35734e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.61791e+11 } } mol +Time: 9.51e+08 s, dt: 4320000 s, Cycle: 241 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-02 ) ( Rwell ) = ( 6.15e-11 ) ( R ) = ( 1.97e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00330667 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582794 s | Solve Time: 0.253044 s + compositionalMultiphaseFlow: Max pressure change: 7843.791 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 74.872 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8979025853127496e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-04 ) ( Rwell ) = ( 5.63e-11 ) ( R ) = ( 1.93e-04 ) + Last LinSolve(iter,res) = ( 3, 3.31e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13813744.784010895 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.98212e+06, 9.26624e+06, 1.03085e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.0404e+06, -1.02628e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.35946e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.53919e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00554e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.35946e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.63914e+11 } } mol +Time: 9.55e+08 s, dt: 4320000 s, Cycle: 242 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-02 ) ( Rwell ) = ( 6.12e-11 ) ( R ) = ( 1.96e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00359354 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585584 s | Solve Time: 0.253131 s + compositionalMultiphaseFlow: Max pressure change: 7843.164 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 73.646 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.514263686108741e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.75e-04 ) ( Rwell ) = ( 5.62e-11 ) ( R ) = ( 2.75e-04 ) + Last LinSolve(iter,res) = ( 3, 3.59e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13820381.036402436 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.98874e+06, 9.27327e+06, 1.03147e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.03269e+06, -1.0201e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.36158e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.54238e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00735e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.36158e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.66037e+11 } } mol +Time: 9.60e+08 s, dt: 4320000 s, Cycle: 243 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-02 ) ( Rwell ) = ( 6.10e-11 ) ( R ) = ( 1.94e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585112 s | Solve Time: 0.252854 s + compositionalMultiphaseFlow: Max pressure change: 7842.709 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 73.306 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.046701423785713e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-04 ) ( Rwell ) = ( 5.60e-11 ) ( R ) = ( 2.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.69e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13827016.326760668 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 8.99537e+06, 9.28031e+06, 1.03208e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.02499e+06, -1.01393e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.36371e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.54556e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.00915e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.36371e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.6816e+11 } } mol +Time: 9.64e+08 s, dt: 4320000 s, Cycle: 244 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-02 ) ( Rwell ) = ( 6.09e-11 ) ( R ) = ( 1.92e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00379704 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586979 s | Solve Time: 0.253957 s + compositionalMultiphaseFlow: Max pressure change: 7842.602 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 72.838 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.704385845346934e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-04 ) ( Rwell ) = ( 5.59e-11 ) ( R ) = ( 2.28e-04 ) + Last LinSolve(iter,res) = ( 3, 3.80e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13833650.298840092 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.00199e+06, 9.28734e+06, 1.0327e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.01728e+06, -1.00776e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.36583e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.54875e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01096e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.36583e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.70283e+11 } } mol +Time: 9.68e+08 s, dt: 4320000 s, Cycle: 245 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-02 ) ( Rwell ) = ( 6.08e-11 ) ( R ) = ( 1.90e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00386508 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585177 s | Solve Time: 0.253524 s + compositionalMultiphaseFlow: Max pressure change: 7841.087 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 72.187 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5788313525444408e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-04 ) ( Rwell ) = ( 5.57e-11 ) ( R ) = ( 1.96e-04 ) + Last LinSolve(iter,res) = ( 3, 3.87e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13840282.734444968 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.00861e+06, 9.29438e+06, 1.03332e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.00957e+06, -1.00158e+06 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.36795e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.55193e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01276e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.36795e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.72406e+11 } } mol +Time: 9.73e+08 s, dt: 4320000 s, Cycle: 246 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-02 ) ( Rwell ) = ( 6.06e-11 ) ( R ) = ( 1.87e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00388501 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585598 s | Solve Time: 0.252862 s + compositionalMultiphaseFlow: Max pressure change: 7840.062 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 71.434 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5152858919842416e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-04 ) ( Rwell ) = ( 5.56e-11 ) ( R ) = ( 1.97e-04 ) + Last LinSolve(iter,res) = ( 3, 3.89e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13846913.403491704 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.01522e+06, 9.30141e+06, 1.03393e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -2.00188e+06, -995413 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 7.99999e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 7.99999e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37008e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.55512e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01456e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37008e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.7453e+11 } } mol +Time: 9.77e+08 s, dt: 1320000 s, Cycle: 247 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.68e-03 ) ( Rwell ) = ( 6.05e-11 ) ( R ) = ( 5.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00974174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585265 s | Solve Time: 0.174454 s + compositionalMultiphaseFlow: Max pressure change: 2376.272 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 21.793 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.948198397350165e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.91e-05 ) ( Rwell ) = ( 5.19e-12 ) ( R ) = ( 5.91e-05 ) + Last LinSolve(iter,res) = ( 2, 9.74e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13848935.222915858 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.01724e+06, 9.30355e+06, 1.03412e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.99519e+06, -989243 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37072e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.55609e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01512e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37072e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.75178e+11 } } mol +Time: 9.78e+08 s, dt: 2640000 s, Cycle: 248 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ( Rwell ) = ( 1.00e-11 ) ( R ) = ( 1.13e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00333738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587574 s | Solve Time: 0.253498 s + compositionalMultiphaseFlow: Max pressure change: 4798.584 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.209 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.877058543823921e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-05 ) ( Rwell ) = ( 2.06e-11 ) ( R ) = ( 3.49e-05 ) + Last LinSolve(iter,res) = ( 3, 3.34e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13852977.485571843 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.02129e+06, 9.30784e+06, 1.0345e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.99315e+06, -987362 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37202e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.55803e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01622e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37202e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.76475e+11 } } mol +Time: 9.81e+08 s, dt: 4320000 s, Cycle: 249 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-02 ) ( Rwell ) = ( 2.55e-11 ) ( R ) = ( 1.85e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00342279 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58945 s | Solve Time: 0.253815 s + compositionalMultiphaseFlow: Max pressure change: 7846.955 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 70.303 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2790960723818579e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-04 ) ( Rwell ) = ( 5.55e-11 ) ( R ) = ( 1.75e-04 ) + Last LinSolve(iter,res) = ( 3, 3.42e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13859613.357959192 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.02791e+06, 9.31487e+06, 1.03512e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.98906e+06, -983600 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37415e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.56122e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01802e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37415e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.78599e+11 } } mol +Time: 9.85e+08 s, dt: 4320000 s, Cycle: 250 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.84e-02 ) ( Rwell ) = ( 6.03e-11 ) ( R ) = ( 1.84e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00346964 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587302 s | Solve Time: 0.25329 s + compositionalMultiphaseFlow: Max pressure change: 7835.392 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 70.069 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2912136575504718e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 5.52e-11 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 3, 3.47e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13866240.945334964 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.03453e+06, 9.3219e+06, 1.03573e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.98237e+06, -977425 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37627e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5644e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.01983e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37627e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.80722e+11 } } mol +Time: 9.90e+08 s, dt: 4320000 s, Cycle: 251 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-02 ) ( Rwell ) = ( 6.00e-11 ) ( R ) = ( 1.82e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00348716 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586057 s | Solve Time: 0.253023 s + compositionalMultiphaseFlow: Max pressure change: 7834.106 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 69.656 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1402277299010777e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-04 ) ( Rwell ) = ( 5.51e-11 ) ( R ) = ( 2.05e-04 ) + Last LinSolve(iter,res) = ( 3, 3.49e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13872866.788234403 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.04114e+06, 9.32892e+06, 1.03635e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.97569e+06, -971257 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.37839e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.56759e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02163e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.37839e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.82845e+11 } } mol +Time: 9.94e+08 s, dt: 4320000 s, Cycle: 252 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-02 ) ( Rwell ) = ( 5.99e-11 ) ( R ) = ( 1.80e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00350143 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586323 s | Solve Time: 0.254321 s + compositionalMultiphaseFlow: Max pressure change: 7831.764 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 69.080 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4000068312425284e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-04 ) ( Rwell ) = ( 5.49e-11 ) ( R ) = ( 2.27e-04 ) + Last LinSolve(iter,res) = ( 3, 3.50e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13879491.386546915 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.04776e+06, 9.33595e+06, 1.03697e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.969e+06, -965090 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.38052e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.57077e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02344e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.38052e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.84968e+11 } } mol +Time: 9.98e+08 s, dt: 4320000 s, Cycle: 253 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.78e-02 ) ( Rwell ) = ( 5.97e-11 ) ( R ) = ( 1.78e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0035726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58966 s | Solve Time: 0.252932 s + compositionalMultiphaseFlow: Max pressure change: 7828.202 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 68.359 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3372881383366675e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-04 ) ( Rwell ) = ( 5.48e-11 ) ( R ) = ( 2.04e-04 ) + Last LinSolve(iter,res) = ( 3, 3.57e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13886115.364853606 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.05437e+06, 9.34297e+06, 1.03758e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.96232e+06, -958924 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.38264e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.57396e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02524e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.38264e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.87092e+11 } } mol +Time: 1.00e+09 s, dt: 4320000 s, Cycle: 254 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-02 ) ( Rwell ) = ( 5.96e-11 ) ( R ) = ( 1.76e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00395036 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589714 s | Solve Time: 0.253078 s + compositionalMultiphaseFlow: Max pressure change: 7825.717 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 67.534 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3825834236369516e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 5.46e-11 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 3, 3.95e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13892737.596425867 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.06098e+06, 9.34998e+06, 1.0382e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.95564e+06, -952758 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.38476e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.57714e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.02705e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.38476e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.89215e+11 } } mol +Time: 1.01e+09 s, dt: 3000000 s, Cycle: 255 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ( Rwell ) = ( 5.95e-11 ) ( R ) = ( 1.22e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00343277 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.777062 s | Solve Time: 0.25368 s + compositionalMultiphaseFlow: Max pressure change: 5422.817 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.592 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0121686833453047e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.20e-05 ) ( Rwell ) = ( 2.62e-11 ) ( R ) = ( 4.20e-05 ) + Last LinSolve(iter,res) = ( 3, 3.43e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13897327.721785394 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.06557e+06, 9.35485e+06, 1.03863e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.94897e+06, -946594 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.38624e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.57935e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0283e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.38624e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.90689e+11 } } mol +Time: 1.01e+09 s, dt: 4320000 s, Cycle: 256 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-02 ) ( Rwell ) = ( 3.10e-11 ) ( R ) = ( 1.74e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00362941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585413 s | Solve Time: 0.252968 s + compositionalMultiphaseFlow: Max pressure change: 7830.410 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66.897 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.57222810660241e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-04 ) ( Rwell ) = ( 5.45e-11 ) ( R ) = ( 1.92e-04 ) + Last LinSolve(iter,res) = ( 3, 3.63e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13903953.181560751 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.07218e+06, 9.36187e+06, 1.03924e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.94433e+06, -942320 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.38836e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.58254e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03011e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.38836e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.92813e+11 } } mol +Time: 1.01e+09 s, dt: 4320000 s, Cycle: 257 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.73e-02 ) ( Rwell ) = ( 5.93e-11 ) ( R ) = ( 1.73e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00367099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58347 s | Solve Time: 0.255029 s + compositionalMultiphaseFlow: Max pressure change: 7816.440 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66.573 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0284981972752405e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.88e-04 ) ( Rwell ) = ( 5.43e-11 ) ( R ) = ( 1.88e-04 ) + Last LinSolve(iter,res) = ( 3, 3.67e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13910572.18912328 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.07879e+06, 9.36889e+06, 1.03986e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.93766e+06, -936152 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39048e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.58573e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03191e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39048e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.94936e+11 } } mol +Time: 1.02e+09 s, dt: 4320000 s, Cycle: 258 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.71e-02 ) ( Rwell ) = ( 5.91e-11 ) ( R ) = ( 1.71e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368042 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586643 s | Solve Time: 0.253368 s + compositionalMultiphaseFlow: Max pressure change: 7816.802 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66.100 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.216360666744798e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 5.41e-11 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 3, 3.68e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13917189.684626453 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.0854e+06, 9.3759e+06, 1.04048e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.93098e+06, -929990 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39261e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.58891e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03371e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39261e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.9706e+11 } } mol +Time: 1.02e+09 s, dt: 4320000 s, Cycle: 259 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-02 ) ( Rwell ) = ( 5.89e-11 ) ( R ) = ( 1.69e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583693 s | Solve Time: 0.252794 s + compositionalMultiphaseFlow: Max pressure change: 7817.057 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 65.495 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.771639335991566e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-04 ) ( Rwell ) = ( 5.40e-11 ) ( R ) = ( 1.62e-04 ) + Last LinSolve(iter,res) = ( 3, 3.68e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13923805.950147653 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.09201e+06, 9.38291e+06, 1.04109e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.92431e+06, -923828 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39473e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.5921e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03552e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39473e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 1.99183e+11 } } mol +Time: 1.03e+09 s, dt: 4320000 s, Cycle: 260 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-02 ) ( Rwell ) = ( 5.88e-11 ) ( R ) = ( 1.66e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00370361 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582698 s | Solve Time: 0.253091 s + compositionalMultiphaseFlow: Max pressure change: 7817.030 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 64.770 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.407985999132507e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-04 ) ( Rwell ) = ( 5.39e-11 ) ( R ) = ( 1.99e-04 ) + Last LinSolve(iter,res) = ( 3, 3.70e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13930420.941008719 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.09861e+06, 9.38992e+06, 1.04171e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.91764e+06, -917668 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39685e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.59528e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03732e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39685e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.01307e+11 } } mol +Time: 1.03e+09 s, dt: 4320000 s, Cycle: 261 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-02 ) ( Rwell ) = ( 5.87e-11 ) ( R ) = ( 1.66e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00382892 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585245 s | Solve Time: 0.253735 s + compositionalMultiphaseFlow: Max pressure change: 7815.251 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 63.940 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.174418387206444e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-04 ) ( Rwell ) = ( 5.37e-11 ) ( R ) = ( 2.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.83e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13937034.366146792 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.10522e+06, 9.39693e+06, 1.04232e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.91097e+06, -911508 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.39898e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.59847e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.03913e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.39898e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.0343e+11 } } mol +Time: 1.04e+09 s, dt: 4320000 s, Cycle: 262 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.65e-02 ) ( Rwell ) = ( 5.85e-11 ) ( R ) = ( 1.65e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00372756 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585803 s | Solve Time: 0.253656 s + compositionalMultiphaseFlow: Max pressure change: 7813.805 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 63.606 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1326253417376364e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-04 ) ( Rwell ) = ( 5.36e-11 ) ( R ) = ( 1.59e-04 ) + Last LinSolve(iter,res) = ( 3, 3.73e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13943645.23225161 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.11182e+06, 9.40393e+06, 1.04294e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.9043e+06, -905349 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.4011e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.60165e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04093e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.4011e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.05553e+11 } } mol +Time: 1.04e+09 s, dt: 1320000 s, Cycle: 263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-03 ) ( Rwell ) = ( 5.84e-11 ) ( R ) = ( 5.00e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00267153 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581209 s | Solve Time: 0.252341 s + compositionalMultiphaseFlow: Max pressure change: 2375.153 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 19.438 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5357126924686604e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-05 ) ( Rwell ) = ( 4.94e-12 ) ( R ) = ( 1.78e-05 ) + Last LinSolve(iter,res) = ( 3, 2.67e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13945656.365272205 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.11383e+06, 9.40607e+06, 1.04313e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.89764e+06, -899192 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40175e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.60262e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04149e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40175e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.06202e+11 } } mol +Time: 1.04e+09 s, dt: 2640000 s, Cycle: 264 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.97e-03 ) ( Rwell ) = ( 9.69e-12 ) ( R ) = ( 9.97e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00331497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58823 s | Solve Time: 0.252883 s + compositionalMultiphaseFlow: Max pressure change: 4780.976 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.744 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.670958604569009e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.23e-05 ) ( Rwell ) = ( 2.00e-11 ) ( R ) = ( 6.23e-05 ) + Last LinSolve(iter,res) = ( 3, 3.31e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13949696.405449191 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.050 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.11787e+06, 9.41035e+06, 1.0435e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.8956e+06, -897319 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40305e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.60457e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04259e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40305e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.075e+11 } } mol +Time: 1.04e+09 s, dt: 4320000 s, Cycle: 265 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-02 ) ( Rwell ) = ( 2.47e-11 ) ( R ) = ( 1.63e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00363561 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582122 s | Solve Time: 0.267359 s + compositionalMultiphaseFlow: Max pressure change: 7822.416 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 63.175 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0322091869463534e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-04 ) ( Rwell ) = ( 5.35e-11 ) ( R ) = ( 1.68e-04 ) + Last LinSolve(iter,res) = ( 3, 3.64e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13956312.341358693 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.12447e+06, 9.41735e+06, 1.04412e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.89153e+06, -893556 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40517e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.60776e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04439e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40517e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.09623e+11 } } mol +Time: 1.05e+09 s, dt: 4320000 s, Cycle: 266 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-02 ) ( Rwell ) = ( 5.82e-11 ) ( R ) = ( 1.61e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00361455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587726 s | Solve Time: 0.253351 s + compositionalMultiphaseFlow: Max pressure change: 7813.784 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 62.877 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.356092347534428e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-04 ) ( Rwell ) = ( 5.32e-11 ) ( R ) = ( 1.44e-04 ) + Last LinSolve(iter,res) = ( 3, 3.61e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13962921.343079347 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.13107e+06, 9.42435e+06, 1.04474e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.88487e+06, -887394 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40729e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.61094e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0462e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40729e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.11747e+11 } } mol +Time: 1.05e+09 s, dt: 4320000 s, Cycle: 267 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-02 ) ( Rwell ) = ( 5.80e-11 ) ( R ) = ( 1.60e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0036226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583036 s | Solve Time: 0.253289 s + compositionalMultiphaseFlow: Max pressure change: 7813.335 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 62.450 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.002750810920389e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-04 ) ( Rwell ) = ( 5.31e-11 ) ( R ) = ( 1.05e-04 ) + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13969528.849581633 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.13767e+06, 9.43135e+06, 1.04535e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.87821e+06, -881238 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.40942e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.61413e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.048e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.40942e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.1387e+11 } } mol +Time: 1.06e+09 s, dt: 4320000 s, Cycle: 268 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-02 ) ( Rwell ) = ( 5.78e-11 ) ( R ) = ( 1.58e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0036323 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587044 s | Solve Time: 0.253497 s + compositionalMultiphaseFlow: Max pressure change: 7812.064 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 61.913 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.404181321390979e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 5.30e-11 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 3, 3.63e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13976135.214093078 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.14426e+06, 9.43835e+06, 1.04597e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.87155e+06, -875083 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41154e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.61731e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.04981e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41154e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.15994e+11 } } mol +Time: 1.06e+09 s, dt: 4320000 s, Cycle: 269 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-02 ) ( Rwell ) = ( 5.77e-11 ) ( R ) = ( 1.58e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00364637 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583468 s | Solve Time: 0.253315 s + compositionalMultiphaseFlow: Max pressure change: 7810.376 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 61.331 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.073913756456719e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-04 ) ( Rwell ) = ( 5.28e-11 ) ( R ) = ( 1.99e-04 ) + Last LinSolve(iter,res) = ( 3, 3.65e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13982740.398842603 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.15086e+06, 9.44534e+06, 1.04658e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.8649e+06, -868929 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41366e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.6205e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05161e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41366e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.18118e+11 } } mol +Time: 1.07e+09 s, dt: 4320000 s, Cycle: 270 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-02 ) ( Rwell ) = ( 5.76e-11 ) ( R ) = ( 1.57e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00367938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586254 s | Solve Time: 0.253316 s + compositionalMultiphaseFlow: Max pressure change: 7807.872 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 61.271 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.754055264541648e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 5.27e-11 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 3, 3.68e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13989344.588898828 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.15745e+06, 9.45234e+06, 1.0472e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.85824e+06, -862775 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41579e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.62368e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05342e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41579e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.20241e+11 } } mol +Time: 1.07e+09 s, dt: 3000000 s, Cycle: 271 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ( Rwell ) = ( 5.74e-11 ) ( R ) = ( 1.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00319146 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5858 s | Solve Time: 0.252981 s + compositionalMultiphaseFlow: Max pressure change: 5413.392 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.488 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.133122380238333e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.26e-05 ) ( Rwell ) = ( 2.53e-11 ) ( R ) = ( 6.26e-05 ) + Last LinSolve(iter,res) = ( 3, 3.19e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 13993924.927136445 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.16203e+06, 9.45719e+06, 1.04762e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.85159e+06, -856622 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41726e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.62589e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05467e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41726e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.21716e+11 } } mol +Time: 1.07e+09 s, dt: 4320000 s, Cycle: 272 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-02 ) ( Rwell ) = ( 3.00e-11 ) ( R ) = ( 1.55e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00381623 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586968 s | Solve Time: 0.252599 s + compositionalMultiphaseFlow: Max pressure change: 7812.690 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 60.901 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.915651008882918e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-04 ) ( Rwell ) = ( 5.26e-11 ) ( R ) = ( 1.60e-04 ) + Last LinSolve(iter,res) = ( 3, 3.82e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14000531.070693139 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.16862e+06, 9.46418e+06, 1.04824e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.84697e+06, -852354 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.41938e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.62908e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05648e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.41938e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.23839e+11 } } mol +Time: 1.08e+09 s, dt: 4320000 s, Cycle: 273 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-02 ) ( Rwell ) = ( 5.73e-11 ) ( R ) = ( 1.54e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00389514 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584613 s | Solve Time: 0.252679 s + compositionalMultiphaseFlow: Max pressure change: 7799.834 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 60.537 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.956394982855386e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.52e-05 ) ( Rwell ) = ( 5.23e-11 ) ( R ) = ( 9.52e-05 ) + Last LinSolve(iter,res) = ( 3, 3.90e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14007131.18825214 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.17521e+06, 9.47117e+06, 1.04885e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.84032e+06, -846199 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42151e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.63226e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.05828e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42151e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.25962e+11 } } mol +Time: 1.08e+09 s, dt: 4320000 s, Cycle: 274 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-02 ) ( Rwell ) = ( 5.71e-11 ) ( R ) = ( 1.52e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00383432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585088 s | Solve Time: 0.252552 s + compositionalMultiphaseFlow: Max pressure change: 7797.442 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 60.062 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.839390443464822e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 5.22e-11 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 3, 3.83e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14013729.242565382 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.1818e+06, 9.47815e+06, 1.04947e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.83367e+06, -840049 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42363e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.63545e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06009e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42363e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.28086e+11 } } mol +Time: 1.09e+09 s, dt: 4320000 s, Cycle: 275 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-02 ) ( Rwell ) = ( 5.69e-11 ) ( R ) = ( 1.51e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00378475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58522 s | Solve Time: 0.253244 s + compositionalMultiphaseFlow: Max pressure change: 7795.338 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 59.500 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.940724782689145e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-04 ) ( Rwell ) = ( 5.21e-11 ) ( R ) = ( 1.07e-04 ) + Last LinSolve(iter,res) = ( 3, 3.78e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14020326.402468942 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.18838e+06, 9.48514e+06, 1.05008e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.82703e+06, -833900 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42575e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.63863e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06189e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42575e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.30209e+11 } } mol +Time: 1.09e+09 s, dt: 4320000 s, Cycle: 276 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-02 ) ( Rwell ) = ( 5.68e-11 ) ( R ) = ( 1.51e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0038679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584946 s | Solve Time: 0.252742 s + compositionalMultiphaseFlow: Max pressure change: 7792.557 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 59.095 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.590404661999116e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-04 ) ( Rwell ) = ( 5.20e-11 ) ( R ) = ( 1.03e-04 ) + Last LinSolve(iter,res) = ( 3, 3.87e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14026922.078640347 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.19497e+06, 9.49212e+06, 1.0507e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.82038e+06, -827752 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.42788e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.64182e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0637e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.42788e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19555e+12, 2.32332e+11 } } mol +Time: 1.09e+09 s, dt: 4320000 s, Cycle: 277 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-02 ) ( Rwell ) = ( 5.67e-11 ) ( R ) = ( 1.50e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00375018 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590854 s | Solve Time: 0.253148 s + compositionalMultiphaseFlow: Max pressure change: 7795.087 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 58.968 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.391923018129631e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-04 ) ( Rwell ) = ( 5.18e-11 ) ( R ) = ( 1.25e-04 ) + Last LinSolve(iter,res) = ( 3, 3.75e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14033516.705500811 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.20155e+06, 9.4991e+06, 1.05131e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.81374e+06, -821605 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.645e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.0655e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.34456e+11 } } mol +Time: 1.10e+09 s, dt: 4320000 s, Cycle: 278 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-02 ) ( Rwell ) = ( 5.65e-11 ) ( R ) = ( 1.49e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00374023 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582786 s | Solve Time: 0.253701 s + compositionalMultiphaseFlow: Max pressure change: 7794.947 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 58.738 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.109169105039669e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 5.17e-11 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 3, 3.74e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14040111.141746152 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.20814e+06, 9.50608e+06, 1.05193e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.8071e+06, -815459 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43212e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.64819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06731e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43212e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.3658e+11 } } mol +Time: 1.10e+09 s, dt: 1320000 s, Cycle: 279 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-03 ) ( Rwell ) = ( 5.64e-11 ) ( R ) = ( 4.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00260778 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586529 s | Solve Time: 0.253133 s + compositionalMultiphaseFlow: Max pressure change: 2370.373 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 17.934 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2933293004446789e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-05 ) ( Rwell ) = ( 4.78e-12 ) ( R ) = ( 1.41e-05 ) + Last LinSolve(iter,res) = ( 3, 2.61e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14042119.733822202 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.21015e+06, 9.50821e+06, 1.05212e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.80045e+06, -809312 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43277e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.64916e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06786e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43277e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.37229e+11 } } mol +Time: 1.10e+09 s, dt: 2640000 s, Cycle: 280 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.97e-03 ) ( Rwell ) = ( 9.46e-12 ) ( R ) = ( 8.97e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00382102 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58804 s | Solve Time: 0.252935 s + compositionalMultiphaseFlow: Max pressure change: 4766.122 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.705 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.963843127730016e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-05 ) ( Rwell ) = ( 1.93e-11 ) ( R ) = ( 3.77e-05 ) + Last LinSolve(iter,res) = ( 3, 3.82e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14046149.533711862 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.21417e+06, 9.51248e+06, 1.05249e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.79843e+06, -807440 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43407e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.65111e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.06896e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43407e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.38526e+11 } } mol +Time: 1.11e+09 s, dt: 4320000 s, Cycle: 281 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-02 ) ( Rwell ) = ( 2.40e-11 ) ( R ) = ( 1.46e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0037671 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583064 s | Solve Time: 0.252562 s + compositionalMultiphaseFlow: Max pressure change: 7800.849 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 58.052 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.749920977435544e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-04 ) ( Rwell ) = ( 5.16e-11 ) ( R ) = ( 1.01e-04 ) + Last LinSolve(iter,res) = ( 3, 3.77e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14052745.664972506 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.22075e+06, 9.51946e+06, 1.05311e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.79437e+06, -803683 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43619e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.65429e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07077e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43619e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.4065e+11 } } mol +Time: 1.11e+09 s, dt: 4320000 s, Cycle: 282 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-02 ) ( Rwell ) = ( 5.63e-11 ) ( R ) = ( 1.45e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00387319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586731 s | Solve Time: 0.253537 s + compositionalMultiphaseFlow: Max pressure change: 7792.383 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 57.678 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.196764555932432e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 5.14e-11 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 3, 3.87e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14059337.463432413 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.22733e+06, 9.52643e+06, 1.05372e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.78773e+06, -797534 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.43832e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.65748e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07257e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.43832e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.42773e+11 } } mol +Time: 1.12e+09 s, dt: 4320000 s, Cycle: 283 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-02 ) ( Rwell ) = ( 5.61e-11 ) ( R ) = ( 1.44e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00361678 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585581 s | Solve Time: 0.25326 s + compositionalMultiphaseFlow: Max pressure change: 7792.622 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 57.408 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.783956632532394e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-04 ) ( Rwell ) = ( 5.12e-11 ) ( R ) = ( 1.09e-04 ) + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14065926.188040724 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.23391e+06, 9.5334e+06, 1.05433e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.78109e+06, -791389 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44044e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.66066e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07437e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44044e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.44896e+11 } } mol +Time: 1.12e+09 s, dt: 4320000 s, Cycle: 284 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-02 ) ( Rwell ) = ( 5.59e-11 ) ( R ) = ( 1.43e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00357444 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58497 s | Solve Time: 0.253112 s + compositionalMultiphaseFlow: Max pressure change: 7791.652 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 57.049 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.930667930087452e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-04 ) ( Rwell ) = ( 5.11e-11 ) ( R ) = ( 1.10e-04 ) + Last LinSolve(iter,res) = ( 3, 3.57e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14072513.905500906 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.24049e+06, 9.54037e+06, 1.05495e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.77446e+06, -785247 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44256e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.66385e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07618e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44256e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.47019e+11 } } mol +Time: 1.12e+09 s, dt: 4320000 s, Cycle: 285 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-02 ) ( Rwell ) = ( 5.58e-11 ) ( R ) = ( 1.43e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00358148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586424 s | Solve Time: 0.252563 s + compositionalMultiphaseFlow: Max pressure change: 7791.007 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 56.641 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.802543446842279e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 5.10e-11 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 3, 3.58e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14079100.377906378 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.24706e+06, 9.54734e+06, 1.05556e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.76782e+06, -779105 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44469e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.66703e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07798e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44469e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.49143e+11 } } mol +Time: 1.13e+09 s, dt: 4320000 s, Cycle: 286 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-02 ) ( Rwell ) = ( 5.56e-11 ) ( R ) = ( 1.43e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00417237 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585593 s | Solve Time: 0.253163 s + compositionalMultiphaseFlow: Max pressure change: 7791.017 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 56.608 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.807324973654659e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-04 ) ( Rwell ) = ( 5.09e-11 ) ( R ) = ( 1.24e-04 ) + Last LinSolve(iter,res) = ( 3, 4.17e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14085686.513730228 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.25364e+06, 9.55431e+06, 1.05618e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.76119e+06, -772963 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44681e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.67022e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.07979e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44681e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.51266e+11 } } mol +Time: 1.13e+09 s, dt: 3000000 s, Cycle: 287 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.85e-03 ) ( Rwell ) = ( 5.55e-11 ) ( R ) = ( 9.85e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00371293 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582994 s | Solve Time: 0.253068 s + compositionalMultiphaseFlow: Max pressure change: 5402.951 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.290 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.896415194801442e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.57e-05 ) ( Rwell ) = ( 2.44e-11 ) ( R ) = ( 7.57e-05 ) + Last LinSolve(iter,res) = ( 3, 3.71e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14090254.708369533 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.2582e+06, 9.55914e+06, 1.0566e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.75456e+06, -766822 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.44828e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.67243e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08104e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.44828e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.5274e+11 } } mol +Time: 1.14e+09 s, dt: 4320000 s, Cycle: 288 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-02 ) ( Rwell ) = ( 2.91e-11 ) ( R ) = ( 1.41e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0041681 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586743 s | Solve Time: 0.252575 s + compositionalMultiphaseFlow: Max pressure change: 7794.781 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 56.393 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.754342432135907e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-04 ) ( Rwell ) = ( 5.07e-11 ) ( R ) = ( 1.10e-04 ) + Last LinSolve(iter,res) = ( 3, 4.17e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14096840.878093656 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.080 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.26477e+06, 9.56611e+06, 1.05722e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.74995e+06, -762562 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.45041e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.67561e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08285e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.45041e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.54864e+11 } } mol +Time: 1.14e+09 s, dt: 4320000 s, Cycle: 289 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-02 ) ( Rwell ) = ( 5.54e-11 ) ( R ) = ( 1.40e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00417317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585507 s | Solve Time: 0.25377 s + compositionalMultiphaseFlow: Max pressure change: 7786.963 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 56.154 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.114249945759042e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-04 ) ( Rwell ) = ( 5.05e-11 ) ( R ) = ( 1.20e-04 ) + Last LinSolve(iter,res) = ( 3, 4.17e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14103423.009763164 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.27135e+06, 9.57307e+06, 1.05783e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.74332e+06, -756420 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.45253e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.6788e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08465e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.45253e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.56987e+11 } } mol +Time: 1.14e+09 s, dt: 4320000 s, Cycle: 290 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-02 ) ( Rwell ) = ( 5.52e-11 ) ( R ) = ( 1.39e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00418494 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587297 s | Solve Time: 0.252843 s + compositionalMultiphaseFlow: Max pressure change: 7785.884 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 55.828 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.057283900018362e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-04 ) ( Rwell ) = ( 5.04e-11 ) ( R ) = ( 1.26e-04 ) + Last LinSolve(iter,res) = ( 3, 4.18e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14110003.880790789 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.27792e+06, 9.58003e+06, 1.05844e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.73669e+06, -750282 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.45465e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.68198e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08646e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.45465e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.59111e+11 } } mol +Time: 1.15e+09 s, dt: 4320000 s, Cycle: 291 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-02 ) ( Rwell ) = ( 5.50e-11 ) ( R ) = ( 1.39e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00408954 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584723 s | Solve Time: 0.252675 s + compositionalMultiphaseFlow: Max pressure change: 7784.819 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 55.413 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.073627480951416e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-04 ) ( Rwell ) = ( 5.03e-11 ) ( R ) = ( 1.14e-04 ) + Last LinSolve(iter,res) = ( 3, 4.09e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14116582.915457528 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.28449e+06, 9.58699e+06, 1.05906e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.73007e+06, -744144 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.45678e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.68517e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.08826e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.45678e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.61234e+11 } } mol +Time: 1.15e+09 s, dt: 4320000 s, Cycle: 292 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ( Rwell ) = ( 5.49e-11 ) ( R ) = ( 1.38e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00386326 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589143 s | Solve Time: 0.25297 s + compositionalMultiphaseFlow: Max pressure change: 7781.846 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 55.157 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.020847123615724e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-04 ) ( Rwell ) = ( 5.02e-11 ) ( R ) = ( 1.06e-04 ) + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14123161.490360487 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.29106e+06, 9.59394e+06, 1.05967e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.72345e+06, -738008 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.4589e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.68835e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09007e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.4589e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.63357e+11 } } mol +Time: 1.16e+09 s, dt: 4320000 s, Cycle: 293 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ( Rwell ) = ( 5.48e-11 ) ( R ) = ( 1.38e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00364866 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58361 s | Solve Time: 0.252924 s + compositionalMultiphaseFlow: Max pressure change: 7780.702 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 55.090 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.482912348002799e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-04 ) ( Rwell ) = ( 5.01e-11 ) ( R ) = ( 1.41e-04 ) + Last LinSolve(iter,res) = ( 3, 3.65e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14129740.028450707 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.29762e+06, 9.6009e+06, 1.06029e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.71683e+06, -731872 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46102e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.69154e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09187e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46102e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.65481e+11 } } mol +Time: 1.16e+09 s, dt: 4320000 s, Cycle: 294 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-02 ) ( Rwell ) = ( 5.47e-11 ) ( R ) = ( 1.37e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00376053 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583398 s | Solve Time: 0.25321 s + compositionalMultiphaseFlow: Max pressure change: 7778.511 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 54.938 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.548118630598452e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 4.99e-11 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 3, 3.76e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14136317.46950581 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.30419e+06, 9.60786e+06, 1.0609e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.71021e+06, -725735 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46315e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.69472e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09368e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46315e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.67604e+11 } } mol +Time: 1.17e+09 s, dt: 1320000 s, Cycle: 295 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-03 ) ( Rwell ) = ( 5.46e-11 ) ( R ) = ( 4.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00269159 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585588 s | Solve Time: 0.252625 s + compositionalMultiphaseFlow: Max pressure change: 2365.530 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 16.777 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1233134906474262e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.08e-06 ) ( Rwell ) = ( 4.63e-12 ) ( R ) = ( 9.08e-06 ) + Last LinSolve(iter,res) = ( 3, 2.69e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14138322.05555274 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.3062e+06, 9.60998e+06, 1.06109e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.70359e+06, -719600 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.4638e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.6957e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09423e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.4638e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.68253e+11 } } mol +Time: 1.17e+09 s, dt: 2640000 s, Cycle: 296 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.26e-03 ) ( Rwell ) = ( 9.23e-12 ) ( R ) = ( 8.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00296863 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587373 s | Solve Time: 0.252778 s + compositionalMultiphaseFlow: Max pressure change: 4757.887 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33.453 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.4549014222839958e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-05 ) ( Rwell ) = ( 1.86e-11 ) ( R ) = ( 4.21e-05 ) + Last LinSolve(iter,res) = ( 3, 2.97e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14142340.390752934 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.31021e+06, 9.61423e+06, 1.06146e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.70157e+06, -717729 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46509e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.69764e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09533e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46509e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.69551e+11 } } mol +Time: 1.17e+09 s, dt: 4320000 s, Cycle: 297 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-02 ) ( Rwell ) = ( 2.32e-11 ) ( R ) = ( 1.35e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00371205 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585264 s | Solve Time: 0.25258 s + compositionalMultiphaseFlow: Max pressure change: 7779.949 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 54.445 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.642347820580042e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-04 ) ( Rwell ) = ( 4.98e-11 ) ( R ) = ( 1.33e-04 ) + Last LinSolve(iter,res) = ( 3, 3.71e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14148919.915611863 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.31677e+06, 9.62118e+06, 1.06207e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.69752e+06, -713981 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46722e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.70083e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09714e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46722e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.71674e+11 } } mol +Time: 1.17e+09 s, dt: 4320000 s, Cycle: 298 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ( Rwell ) = ( 5.44e-11 ) ( R ) = ( 1.34e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00376952 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585189 s | Solve Time: 0.25342 s + compositionalMultiphaseFlow: Max pressure change: 7773.326 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 54.090 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.3785854453304296e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-04 ) ( Rwell ) = ( 4.96e-11 ) ( R ) = ( 1.22e-04 ) + Last LinSolve(iter,res) = ( 3, 3.77e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14155494.205577925 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.32334e+06, 9.62813e+06, 1.06269e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.69091e+06, -707842 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.46934e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.70401e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.09894e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.46934e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.73798e+11 } } mol +Time: 1.18e+09 s, dt: 4320000 s, Cycle: 299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ( Rwell ) = ( 5.42e-11 ) ( R ) = ( 1.33e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00379158 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585087 s | Solve Time: 0.252669 s + compositionalMultiphaseFlow: Max pressure change: 7774.084 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.700 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.054824058214891e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.55e-05 ) ( Rwell ) = ( 4.95e-11 ) ( R ) = ( 9.55e-05 ) + Last LinSolve(iter,res) = ( 3, 3.79e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14162066.870410567 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.3299e+06, 9.63508e+06, 1.0633e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.6843e+06, -701709 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47147e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.7072e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10075e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47147e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.75921e+11 } } mol +Time: 1.18e+09 s, dt: 4320000 s, Cycle: 300 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-02 ) ( Rwell ) = ( 5.41e-11 ) ( R ) = ( 1.32e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00380313 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586814 s | Solve Time: 0.252802 s + compositionalMultiphaseFlow: Max pressure change: 7774.458 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.561 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.762960597564202e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.45e-05 ) ( Rwell ) = ( 4.94e-11 ) ( R ) = ( 9.45e-05 ) + Last LinSolve(iter,res) = ( 3, 3.80e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14168638.547441937 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.33646e+06, 9.64202e+06, 1.06391e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.67768e+06, -695576 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47359e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.71038e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10255e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47359e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.78045e+11 } } mol +Time: 1.19e+09 s, dt: 4320000 s, Cycle: 301 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ( Rwell ) = ( 5.40e-11 ) ( R ) = ( 1.31e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00388212 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59098 s | Solve Time: 0.252568 s + compositionalMultiphaseFlow: Max pressure change: 7774.851 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.353 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.719306578275905e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-04 ) ( Rwell ) = ( 4.92e-11 ) ( R ) = ( 1.02e-04 ) + Last LinSolve(iter,res) = ( 3, 3.88e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14175208.366905592 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.34302e+06, 9.64897e+06, 1.06453e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.67107e+06, -689444 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47571e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.71357e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10435e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47571e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.80168e+11 } } mol +Time: 1.19e+09 s, dt: 4320000 s, Cycle: 302 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ( Rwell ) = ( 5.38e-11 ) ( R ) = ( 1.31e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00401888 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585278 s | Solve Time: 0.25287 s + compositionalMultiphaseFlow: Max pressure change: 7773.711 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.080 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.6442618600585064e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-04 ) ( Rwell ) = ( 4.91e-11 ) ( R ) = ( 1.06e-04 ) + Last LinSolve(iter,res) = ( 3, 4.02e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14181778.326645289 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.34958e+06, 9.65591e+06, 1.06514e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.66446e+06, -683313 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47784e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.71675e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10616e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47784e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.82292e+11 } } mol +Time: 1.20e+09 s, dt: 3000000 s, Cycle: 303 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.09e-03 ) ( Rwell ) = ( 5.37e-11 ) ( R ) = ( 9.09e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00349039 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585821 s | Solve Time: 0.252898 s + compositionalMultiphaseFlow: Max pressure change: 5392.461 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.754 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.0521647130551415e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-05 ) ( Rwell ) = ( 2.36e-11 ) ( R ) = ( 3.98e-05 ) + Last LinSolve(iter,res) = ( 3, 3.49e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14186336.81192883 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.35413e+06, 9.66072e+06, 1.06557e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.65785e+06, -677182 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.47931e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.71897e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10741e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.47931e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.83766e+11 } } mol +Time: 1.20e+09 s, dt: 4320000 s, Cycle: 304 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ( Rwell ) = ( 2.82e-11 ) ( R ) = ( 1.31e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00399741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585129 s | Solve Time: 0.252961 s + compositionalMultiphaseFlow: Max pressure change: 7778.846 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 52.924 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.907782131830963e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ( Rwell ) = ( 4.90e-11 ) ( R ) = ( 1.21e-04 ) + Last LinSolve(iter,res) = ( 3, 4.00e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14192906.207452795 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.36069e+06, 9.66767e+06, 1.06618e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.65326e+06, -672928 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48143e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.72215e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.10922e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48143e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.85889e+11 } } mol +Time: 1.20e+09 s, dt: 4320000 s, Cycle: 305 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-02 ) ( Rwell ) = ( 5.36e-11 ) ( R ) = ( 1.30e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00384139 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585152 s | Solve Time: 0.252888 s + compositionalMultiphaseFlow: Max pressure change: 7773.571 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 52.863 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.613762797893827e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.93e-05 ) ( Rwell ) = ( 4.88e-11 ) ( R ) = ( 9.93e-05 ) + Last LinSolve(iter,res) = ( 3, 3.84e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14199472.337251052 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.36724e+06, 9.6746e+06, 1.06679e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.64665e+06, -666797 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48356e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.72534e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11102e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48356e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.88013e+11 } } mol +Time: 1.21e+09 s, dt: 4320000 s, Cycle: 306 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.29e-02 ) ( Rwell ) = ( 5.34e-11 ) ( R ) = ( 1.29e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00384449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588336 s | Solve Time: 0.252941 s + compositionalMultiphaseFlow: Max pressure change: 7773.105 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 52.728 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.5319423685731266e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.91e-05 ) ( Rwell ) = ( 4.87e-11 ) ( R ) = ( 9.91e-05 ) + Last LinSolve(iter,res) = ( 3, 3.84e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14206037.526675306 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.3738e+06, 9.68154e+06, 1.0674e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.64004e+06, -660668 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48568e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.72852e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11283e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48568e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.90136e+11 } } mol +Time: 1.21e+09 s, dt: 4320000 s, Cycle: 307 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-02 ) ( Rwell ) = ( 5.33e-11 ) ( R ) = ( 1.28e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00385201 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584388 s | Solve Time: 0.252705 s + compositionalMultiphaseFlow: Max pressure change: 7772.454 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 52.526 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.247632272580404e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.89e-05 ) ( Rwell ) = ( 4.86e-11 ) ( R ) = ( 9.89e-05 ) + Last LinSolve(iter,res) = ( 3, 3.85e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14212601.662181243 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.38035e+06, 9.68847e+06, 1.06802e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.63344e+06, -654541 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.4878e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.73171e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11463e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.4878e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.9226e+11 } } mol +Time: 1.22e+09 s, dt: 4320000 s, Cycle: 308 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-02 ) ( Rwell ) = ( 5.32e-11 ) ( R ) = ( 1.28e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00385121 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599237 s | Solve Time: 0.252863 s + compositionalMultiphaseFlow: Max pressure change: 7770.773 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 52.254 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.039404083444609e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-04 ) ( Rwell ) = ( 4.85e-11 ) ( R ) = ( 1.07e-04 ) + Last LinSolve(iter,res) = ( 3, 3.85e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14219164.069669493 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.3869e+06, 9.69541e+06, 1.06863e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.62683e+06, -648413 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.48993e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.73489e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11644e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.48993e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.94383e+11 } } mol +Time: 1.22e+09 s, dt: 4320000 s, Cycle: 309 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-02 ) ( Rwell ) = ( 5.30e-11 ) ( R ) = ( 1.28e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00385569 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583865 s | Solve Time: 0.252794 s + compositionalMultiphaseFlow: Max pressure change: 7770.299 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.961 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.8143334246676375e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-04 ) ( Rwell ) = ( 4.84e-11 ) ( R ) = ( 1.07e-04 ) + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14225726.075028745 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.39345e+06, 9.70234e+06, 1.06924e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.62023e+06, -642287 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49205e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.73808e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.11824e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49205e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.96506e+11 } } mol +Time: 1.23e+09 s, dt: 4320000 s, Cycle: 310 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.27e-02 ) ( Rwell ) = ( 5.29e-11 ) ( R ) = ( 1.27e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00389117 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585467 s | Solve Time: 0.25309 s + compositionalMultiphaseFlow: Max pressure change: 7768.554 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.937 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.455592271217611e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-04 ) ( Rwell ) = ( 4.83e-11 ) ( R ) = ( 1.02e-04 ) + Last LinSolve(iter,res) = ( 3, 3.89e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14232287.841723386 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.4e+06, 9.70927e+06, 1.06986e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.61363e+06, -636162 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49417e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.74126e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12005e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49417e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.9863e+11 } } mol +Time: 1.23e+09 s, dt: 1320000 s, Cycle: 311 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-03 ) ( Rwell ) = ( 5.28e-11 ) ( R ) = ( 3.88e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00280893 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58465 s | Solve Time: 0.252839 s + compositionalMultiphaseFlow: Max pressure change: 2361.061 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 15.878 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.999022061224494e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.26e-06 ) ( Rwell ) = ( 4.48e-12 ) ( R ) = ( 9.26e-06 ) + Last LinSolve(iter,res) = ( 3, 2.81e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14234288.510552201 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.402e+06, 9.71138e+06, 1.07004e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.60703e+06, -630036 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49482e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.74223e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.1206e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49482e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 2.99278e+11 } } mol +Time: 1.23e+09 s, dt: 2640000 s, Cycle: 312 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.73e-03 ) ( Rwell ) = ( 9.01e-12 ) ( R ) = ( 7.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00305929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583849 s | Solve Time: 0.252806 s + compositionalMultiphaseFlow: Max pressure change: 4752.160 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 31.713 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0673307682693718e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.02e-05 ) ( Rwell ) = ( 1.80e-11 ) ( R ) = ( 3.02e-05 ) + Last LinSolve(iter,res) = ( 3, 3.06e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14238296.462163081 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.406e+06, 9.71561e+06, 1.07042e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.60501e+06, -628167 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49612e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.74418e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.1217e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49612e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.00576e+11 } } mol +Time: 1.23e+09 s, dt: 4320000 s, Cycle: 313 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-02 ) ( Rwell ) = ( 2.25e-11 ) ( R ) = ( 1.26e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00387499 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585186 s | Solve Time: 0.252863 s + compositionalMultiphaseFlow: Max pressure change: 7772.765 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.787 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.844439044528805e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-04 ) ( Rwell ) = ( 4.81e-11 ) ( R ) = ( 1.10e-04 ) + Last LinSolve(iter,res) = ( 3, 3.87e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14244857.606478628 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.41255e+06, 9.72254e+06, 1.07103e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.60098e+06, -624426 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.49824e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.74737e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12351e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.49824e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.02699e+11 } } mol +Time: 1.24e+09 s, dt: 4320000 s, Cycle: 314 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-02 ) ( Rwell ) = ( 5.26e-11 ) ( R ) = ( 1.25e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00445746 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586433 s | Solve Time: 0.25303 s + compositionalMultiphaseFlow: Max pressure change: 7764.355 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.565 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.1783101090153707e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.73e-05 ) ( Rwell ) = ( 4.80e-11 ) ( R ) = ( 7.73e-05 ) + Last LinSolve(iter,res) = ( 3, 4.46e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14251417.502578624 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.4191e+06, 9.72946e+06, 1.07164e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.59438e+06, -618300 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50037e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.75055e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12531e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50037e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.04823e+11 } } mol +Time: 1.24e+09 s, dt: 4320000 s, Cycle: 315 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-02 ) ( Rwell ) = ( 5.25e-11 ) ( R ) = ( 1.24e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00448386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586199 s | Solve Time: 0.252893 s + compositionalMultiphaseFlow: Max pressure change: 7762.502 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.318 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.307628527737805e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.32e-05 ) ( Rwell ) = ( 4.78e-11 ) ( R ) = ( 7.32e-05 ) + Last LinSolve(iter,res) = ( 3, 4.48e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14257974.247150399 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.42565e+06, 9.73639e+06, 1.07225e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.58778e+06, -612174 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50249e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.75374e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12712e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50249e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.06946e+11 } } mol +Time: 1.25e+09 s, dt: 4320000 s, Cycle: 316 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-02 ) ( Rwell ) = ( 5.24e-11 ) ( R ) = ( 1.24e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00450527 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58334 s | Solve Time: 0.253377 s + compositionalMultiphaseFlow: Max pressure change: 7760.064 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.013 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2976379737981176e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.30e-05 ) ( Rwell ) = ( 4.77e-11 ) ( R ) = ( 7.30e-05 ) + Last LinSolve(iter,res) = ( 3, 4.51e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14264529.804080699 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.43219e+06, 9.74331e+06, 1.07287e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.58118e+06, -606052 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50461e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.75692e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.12892e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50461e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.0907e+11 } } mol +Time: 1.25e+09 s, dt: 4320000 s, Cycle: 317 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ( Rwell ) = ( 5.22e-11 ) ( R ) = ( 1.23e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00394615 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58626 s | Solve Time: 0.253833 s + compositionalMultiphaseFlow: Max pressure change: 7756.962 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.686 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.387896684303726e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.76e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.95e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14271082.80071889 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.43873e+06, 9.75023e+06, 1.07348e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.57458e+06, -599930 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50674e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.76011e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13073e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50674e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.11193e+11 } } mol +Time: 1.26e+09 s, dt: 4320000 s, Cycle: 318 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ( Rwell ) = ( 5.21e-11 ) ( R ) = ( 1.23e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00414232 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583717 s | Solve Time: 0.252789 s + compositionalMultiphaseFlow: Max pressure change: 7756.570 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.645 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.315156359429139e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.90e-05 ) ( Rwell ) = ( 4.75e-11 ) ( R ) = ( 8.90e-05 ) + Last LinSolve(iter,res) = ( 3, 4.14e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14277637.348357271 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.44527e+06, 9.75714e+06, 1.07409e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.56799e+06, -593810 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.50886e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.76329e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13253e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.50886e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.13317e+11 } } mol +Time: 1.26e+09 s, dt: 3000000 s, Cycle: 319 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.50e-03 ) ( Rwell ) = ( 5.20e-11 ) ( R ) = ( 8.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00338522 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587862 s | Solve Time: 0.254548 s + compositionalMultiphaseFlow: Max pressure change: 5381.258 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.130 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.461993304978208e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.17e-05 ) ( Rwell ) = ( 2.28e-11 ) ( R ) = ( 4.17e-05 ) + Last LinSolve(iter,res) = ( 3, 3.39e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14282185.242959762 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.44982e+06, 9.76195e+06, 1.07451e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.5614e+06, -587689 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51033e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.7655e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13378e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51033e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.14791e+11 } } mol +Time: 1.26e+09 s, dt: 4320000 s, Cycle: 320 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ( Rwell ) = ( 2.73e-11 ) ( R ) = ( 1.22e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00424826 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583782 s | Solve Time: 0.252703 s + compositionalMultiphaseFlow: Max pressure change: 7762.447 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.433 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.351777069395602e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.44e-05 ) ( Rwell ) = ( 4.74e-11 ) ( R ) = ( 9.44e-05 ) + Last LinSolve(iter,res) = ( 3, 4.25e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14288739.781909011 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.45636e+06, 9.76886e+06, 1.07513e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.55682e+06, -583441 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51246e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.76869e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13559e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51246e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.16915e+11 } } mol +Time: 1.27e+09 s, dt: 4320000 s, Cycle: 321 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ( Rwell ) = ( 5.19e-11 ) ( R ) = ( 1.22e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00410098 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589015 s | Solve Time: 0.2536 s + compositionalMultiphaseFlow: Max pressure change: 7756.922 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.247 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.176996273834831e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.81e-05 ) ( Rwell ) = ( 4.72e-11 ) ( R ) = ( 9.81e-05 ) + Last LinSolve(iter,res) = ( 3, 4.10e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14295290.90186906 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.46289e+06, 9.77578e+06, 1.07574e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.55023e+06, -577319 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51458e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.77187e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.13739e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51458e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.19038e+11 } } mol +Time: 1.27e+09 s, dt: 4320000 s, Cycle: 322 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ( Rwell ) = ( 5.17e-11 ) ( R ) = ( 1.22e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00398516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584884 s | Solve Time: 0.253193 s + compositionalMultiphaseFlow: Max pressure change: 7759.180 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.114 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.095565107580356e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.87e-05 ) ( Rwell ) = ( 4.71e-11 ) ( R ) = ( 9.87e-05 ) + Last LinSolve(iter,res) = ( 3, 3.99e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14301840.620912198 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.46943e+06, 9.78269e+06, 1.07635e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.54364e+06, -571200 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.5167e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.77506e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.1392e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.5167e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.21162e+11 } } mol +Time: 1.28e+09 s, dt: 4320000 s, Cycle: 323 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-02 ) ( Rwell ) = ( 5.16e-11 ) ( R ) = ( 1.21e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00398977 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585358 s | Solve Time: 0.25259 s + compositionalMultiphaseFlow: Max pressure change: 7759.164 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.130 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.6324563712497593e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.85e-05 ) ( Rwell ) = ( 4.70e-11 ) ( R ) = ( 9.85e-05 ) + Last LinSolve(iter,res) = ( 3, 3.99e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14308389.747018777 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.47597e+06, 9.7896e+06, 1.07696e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.53705e+06, -565082 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.51883e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.77824e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.141e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.51883e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.23285e+11 } } mol +Time: 1.28e+09 s, dt: 4320000 s, Cycle: 324 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-02 ) ( Rwell ) = ( 5.15e-11 ) ( R ) = ( 1.21e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00399468 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585787 s | Solve Time: 0.253047 s + compositionalMultiphaseFlow: Max pressure change: 7759.076 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.085 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0948878193548524e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-04 ) ( Rwell ) = ( 4.69e-11 ) ( R ) = ( 1.06e-04 ) + Last LinSolve(iter,res) = ( 3, 3.99e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14314938.041122722 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.4825e+06, 9.79651e+06, 1.07757e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.53046e+06, -558964 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52095e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.78143e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14281e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52095e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.25409e+11 } } mol +Time: 1.28e+09 s, dt: 4320000 s, Cycle: 325 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-02 ) ( Rwell ) = ( 5.14e-11 ) ( R ) = ( 1.20e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00362321 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589579 s | Solve Time: 0.253332 s + compositionalMultiphaseFlow: Max pressure change: 7757.712 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.972 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0070623202593794e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-04 ) ( Rwell ) = ( 4.68e-11 ) ( R ) = ( 1.03e-04 ) + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14321485.446870666 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.48904e+06, 9.80341e+06, 1.07819e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.52387e+06, -552846 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52307e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.78461e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14461e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52307e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.27532e+11 } } mol +Time: 1.29e+09 s, dt: 4320000 s, Cycle: 326 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-02 ) ( Rwell ) = ( 5.13e-11 ) ( R ) = ( 1.20e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00367448 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58677 s | Solve Time: 0.253022 s + compositionalMultiphaseFlow: Max pressure change: 7757.152 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.805 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.1385165844000085e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.67e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.67e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14328030.672591895 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.49557e+06, 9.81032e+06, 1.0788e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.51728e+06, -546729 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.5252e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.7878e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14642e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.5252e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.29655e+11 } } mol +Time: 1.29e+09 s, dt: 1320000 s, Cycle: 327 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-03 ) ( Rwell ) = ( 5.11e-11 ) ( R ) = ( 3.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00964434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586174 s | Solve Time: 0.174064 s + compositionalMultiphaseFlow: Max pressure change: 2355.199 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 15.234 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.139051723838776e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-05 ) ( Rwell ) = ( 4.40e-12 ) ( R ) = ( 4.59e-05 ) + Last LinSolve(iter,res) = ( 2, 9.64e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14330036.321837604 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.49756e+06, 9.81242e+06, 1.07899e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.5107e+06, -540614 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52585e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.78877e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14697e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52585e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.30304e+11 } } mol +Time: 1.29e+09 s, dt: 2640000 s, Cycle: 328 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.29e-03 ) ( Rwell ) = ( 8.88e-12 ) ( R ) = ( 7.29e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00318914 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584579 s | Solve Time: 0.253008 s + compositionalMultiphaseFlow: Max pressure change: 4746.852 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 30.342 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8064851828046855e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-05 ) ( Rwell ) = ( 1.73e-11 ) ( R ) = ( 2.87e-05 ) + Last LinSolve(iter,res) = ( 3, 3.19e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14334027.122782275 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.50156e+06, 9.81664e+06, 1.07936e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.50869e+06, -538740 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52714e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.79072e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14807e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52714e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.31601e+11 } } mol +Time: 1.30e+09 s, dt: 4320000 s, Cycle: 329 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-02 ) ( Rwell ) = ( 2.18e-11 ) ( R ) = ( 1.19e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00386454 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585111 s | Solve Time: 0.25302 s + compositionalMultiphaseFlow: Max pressure change: 7762.593 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.539 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.209315595473441e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-04 ) ( Rwell ) = ( 4.65e-11 ) ( R ) = ( 1.09e-04 ) + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14340571.356946183 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.50809e+06, 9.82355e+06, 1.07997e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.50467e+06, -535011 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.52927e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.7939e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.14988e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.52927e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.33725e+11 } } mol +Time: 1.30e+09 s, dt: 4320000 s, Cycle: 330 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-02 ) ( Rwell ) = ( 5.10e-11 ) ( R ) = ( 1.19e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00388346 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584182 s | Solve Time: 0.253242 s + compositionalMultiphaseFlow: Max pressure change: 7755.957 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.543 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0063461120555246e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-04 ) ( Rwell ) = ( 4.64e-11 ) ( R ) = ( 1.10e-04 ) + Last LinSolve(iter,res) = ( 3, 3.88e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14347115.121039733 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.51462e+06, 9.83045e+06, 1.08058e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.49808e+06, -528896 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53139e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.79709e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.15168e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53139e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.35849e+11 } } mol +Time: 1.31e+09 s, dt: 4320000 s, Cycle: 331 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-02 ) ( Rwell ) = ( 5.08e-11 ) ( R ) = ( 1.18e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00389391 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583969 s | Solve Time: 0.253789 s + compositionalMultiphaseFlow: Max pressure change: 7755.869 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.485 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.967927338337617e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-04 ) ( Rwell ) = ( 4.63e-11 ) ( R ) = ( 1.10e-04 ) + Last LinSolve(iter,res) = ( 3, 3.89e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14353657.908602063 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.52115e+06, 9.83735e+06, 1.08119e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.4915e+06, -522781 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53352e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.80027e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.15349e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53352e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.37973e+11 } } mol +Time: 1.31e+09 s, dt: 4320000 s, Cycle: 332 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-02 ) ( Rwell ) = ( 5.07e-11 ) ( R ) = ( 1.18e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0037032 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.629974 s | Solve Time: 0.253991 s + compositionalMultiphaseFlow: Max pressure change: 7754.646 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.325 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9246103638858045e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-04 ) ( Rwell ) = ( 4.62e-11 ) ( R ) = ( 1.03e-04 ) + Last LinSolve(iter,res) = ( 3, 3.70e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14360200.54631982 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.52768e+06, 9.84424e+06, 1.0818e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.48492e+06, -516667 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53564e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.80346e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.15529e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53564e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.40096e+11 } } mol +Time: 1.31e+09 s, dt: 4320000 s, Cycle: 333 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-02 ) ( Rwell ) = ( 5.06e-11 ) ( R ) = ( 1.17e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00362629 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58305 s | Solve Time: 0.253424 s + compositionalMultiphaseFlow: Max pressure change: 7752.305 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.198 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0095422298703767e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-04 ) ( Rwell ) = ( 4.61e-11 ) ( R ) = ( 1.09e-04 ) + Last LinSolve(iter,res) = ( 3, 3.63e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14366740.668263743 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.53421e+06, 9.85114e+06, 1.08241e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.47835e+06, -510553 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53776e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.80664e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.1571e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53776e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.42219e+11 } } mol +Time: 1.32e+09 s, dt: 4320000 s, Cycle: 334 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ( Rwell ) = ( 5.05e-11 ) ( R ) = ( 1.16e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00364971 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583895 s | Solve Time: 0.252953 s + compositionalMultiphaseFlow: Max pressure change: 7751.346 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.985 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.917698197490992e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-04 ) ( Rwell ) = ( 4.60e-11 ) ( R ) = ( 1.08e-04 ) + Last LinSolve(iter,res) = ( 3, 3.65e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14373279.866900872 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.54073e+06, 9.85803e+06, 1.08303e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.47177e+06, -504440 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.53989e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.80983e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.1589e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.53989e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.44343e+11 } } mol +Time: 1.32e+09 s, dt: 3000000 s, Cycle: 335 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.08e-03 ) ( Rwell ) = ( 5.04e-11 ) ( R ) = ( 8.08e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00344986 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583799 s | Solve Time: 0.253305 s + compositionalMultiphaseFlow: Max pressure change: 5376.478 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33.882 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.077844862810821e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-05 ) ( Rwell ) = ( 2.21e-11 ) ( R ) = ( 3.64e-05 ) + Last LinSolve(iter,res) = ( 3, 3.45e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14377819.377269417 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.053 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.54527e+06, 9.86282e+06, 1.08345e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.4652e+06, -498329 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54136e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.81204e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16016e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54136e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.45817e+11 } } mol +Time: 1.33e+09 s, dt: 4320000 s, Cycle: 336 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ( Rwell ) = ( 2.65e-11 ) ( R ) = ( 1.16e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00367436 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588391 s | Solve Time: 0.253471 s + compositionalMultiphaseFlow: Max pressure change: 7755.043 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.522 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.934060770955817e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-04 ) ( Rwell ) = ( 4.58e-11 ) ( R ) = ( 1.01e-04 ) + Last LinSolve(iter,res) = ( 3, 3.67e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14384357.801910445 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.55179e+06, 9.86971e+06, 1.08406e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.46063e+06, -494086 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54348e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.81523e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16196e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54348e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.47941e+11 } } mol +Time: 1.33e+09 s, dt: 4320000 s, Cycle: 337 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ( Rwell ) = ( 5.03e-11 ) ( R ) = ( 1.16e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00366285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588925 s | Solve Time: 0.253888 s + compositionalMultiphaseFlow: Max pressure change: 7746.127 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.533 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.924364307377303e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-04 ) ( Rwell ) = ( 4.57e-11 ) ( R ) = ( 1.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.66e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14390893.995837742 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.55831e+06, 9.8766e+06, 1.08467e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.45406e+06, -487974 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54561e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.81841e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16377e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54561e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.50064e+11 } } mol +Time: 1.33e+09 s, dt: 4320000 s, Cycle: 338 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-02 ) ( Rwell ) = ( 5.01e-11 ) ( R ) = ( 1.15e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00367651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582029 s | Solve Time: 0.252673 s + compositionalMultiphaseFlow: Max pressure change: 7744.659 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.474 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.820936001457497e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-04 ) ( Rwell ) = ( 4.56e-11 ) ( R ) = ( 1.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.68e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14397429.526322091 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.56483e+06, 9.88349e+06, 1.08528e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.44749e+06, -481864 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54773e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.8216e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16557e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54773e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.52187e+11 } } mol +Time: 1.34e+09 s, dt: 4320000 s, Cycle: 339 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-02 ) ( Rwell ) = ( 5.00e-11 ) ( R ) = ( 1.15e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00368659 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58372 s | Solve Time: 0.253976 s + compositionalMultiphaseFlow: Max pressure change: 7742.551 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.374 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.777352331451155e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-04 ) ( Rwell ) = ( 4.55e-11 ) ( R ) = ( 1.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.69e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14403964.02910168 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.57136e+06, 9.89037e+06, 1.08589e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.44092e+06, -475755 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.54985e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.82478e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16738e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.54985e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.5431e+11 } } mol +Time: 1.34e+09 s, dt: 4320000 s, Cycle: 340 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-02 ) ( Rwell ) = ( 4.99e-11 ) ( R ) = ( 1.14e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00369398 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585019 s | Solve Time: 0.253082 s + compositionalMultiphaseFlow: Max pressure change: 7742.324 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.266 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.764281497036336e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-04 ) ( Rwell ) = ( 4.54e-11 ) ( R ) = ( 1.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.69e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14410497.520126378 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.57787e+06, 9.89726e+06, 1.08651e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.43436e+06, -469646 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55198e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.82797e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.16918e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55198e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.56434e+11 } } mol +Time: 1.35e+09 s, dt: 4320000 s, Cycle: 341 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-02 ) ( Rwell ) = ( 4.98e-11 ) ( R ) = ( 1.14e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00369896 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58362 s | Solve Time: 0.25379 s + compositionalMultiphaseFlow: Max pressure change: 7742.905 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.117 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.77301348439174e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-04 ) ( Rwell ) = ( 4.53e-11 ) ( R ) = ( 1.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.70e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14417030.025071569 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.58439e+06, 9.90414e+06, 1.08712e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.42779e+06, -463537 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.5541e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.83115e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17098e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.5541e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.58557e+11 } } mol +Time: 1.35e+09 s, dt: 4320000 s, Cycle: 342 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-02 ) ( Rwell ) = ( 4.97e-11 ) ( R ) = ( 1.14e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.003706 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582384 s | Solve Time: 0.25313 s + compositionalMultiphaseFlow: Max pressure change: 7743.374 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.070 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.784939213684723e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-04 ) ( Rwell ) = ( 4.52e-11 ) ( R ) = ( 1.12e-04 ) + Last LinSolve(iter,res) = ( 3, 3.71e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14423561.544678615 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.59091e+06, 9.91102e+06, 1.08773e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.42122e+06, -457430 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55622e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.83434e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17279e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55622e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.6068e+11 } } mol +Time: 1.36e+09 s, dt: 1320000 s, Cycle: 343 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.48e-03 ) ( Rwell ) = ( 4.96e-11 ) ( R ) = ( 3.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00238473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583534 s | Solve Time: 0.253593 s + compositionalMultiphaseFlow: Max pressure change: 2357.031 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 14.708 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 8.442166615552082e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-06 ) ( Rwell ) = ( 4.20e-12 ) ( R ) = ( 6.76e-06 ) + Last LinSolve(iter,res) = ( 3, 2.38e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14425555.940426353 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.5929e+06, 9.91312e+06, 1.08791e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.41466e+06, -451323 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55687e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.83531e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17334e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55687e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.61329e+11 } } mol +Time: 1.36e+09 s, dt: 2640000 s, Cycle: 344 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-03 ) ( Rwell ) = ( 8.61e-12 ) ( R ) = ( 6.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00341116 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584923 s | Solve Time: 0.253105 s + compositionalMultiphaseFlow: Max pressure change: 4734.834 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29.414 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5941823226238725e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-05 ) ( Rwell ) = ( 1.68e-11 ) ( R ) = ( 2.60e-05 ) + Last LinSolve(iter,res) = ( 3, 3.41e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14429545.931349259 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.59689e+06, 9.91732e+06, 1.08829e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.41265e+06, -449458 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.55817e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.83725e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17444e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.55817e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.62626e+11 } } mol +Time: 1.36e+09 s, dt: 4320000 s, Cycle: 345 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ( Rwell ) = ( 2.12e-11 ) ( R ) = ( 1.13e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00365726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583267 s | Solve Time: 0.252443 s + compositionalMultiphaseFlow: Max pressure change: 7749.325 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.076 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.793548395804926e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-04 ) ( Rwell ) = ( 4.50e-11 ) ( R ) = ( 1.01e-04 ) + Last LinSolve(iter,res) = ( 3, 3.66e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14436076.966997704 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.6034e+06, 9.9242e+06, 1.0889e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.40864e+06, -445727 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56029e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.84044e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17625e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56029e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.6475e+11 } } mol +Time: 1.36e+09 s, dt: 4320000 s, Cycle: 346 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ( Rwell ) = ( 4.94e-11 ) ( R ) = ( 1.13e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00370351 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582797 s | Solve Time: 0.253485 s + compositionalMultiphaseFlow: Max pressure change: 7744.485 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.003 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.721188785415052e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-04 ) ( Rwell ) = ( 4.49e-11 ) ( R ) = ( 1.01e-04 ) + Last LinSolve(iter,res) = ( 3, 3.70e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14442606.48602186 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.60992e+06, 9.93108e+06, 1.08951e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.40208e+06, -439620 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56242e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.84363e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17805e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56242e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.66874e+11 } } mol +Time: 1.37e+09 s, dt: 4320000 s, Cycle: 347 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ( Rwell ) = ( 4.93e-11 ) ( R ) = ( 1.13e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00371703 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588979 s | Solve Time: 0.252787 s + compositionalMultiphaseFlow: Max pressure change: 7745.191 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.876 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7139593195002476e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.48e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.72e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14449135.029886868 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.61643e+06, 9.93795e+06, 1.09012e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.39551e+06, -433514 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56454e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.84681e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.17986e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56454e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.68997e+11 } } mol +Time: 1.37e+09 s, dt: 4320000 s, Cycle: 348 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ( Rwell ) = ( 4.92e-11 ) ( R ) = ( 1.13e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00371608 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58538 s | Solve Time: 0.254744 s + compositionalMultiphaseFlow: Max pressure change: 7745.062 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.705 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.716777991462749e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.47e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.72e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14455662.660103226 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.62295e+06, 9.94483e+06, 1.09073e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.38895e+06, -427408 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56666e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.85e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18166e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56666e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.71121e+11 } } mol +Time: 1.38e+09 s, dt: 4320000 s, Cycle: 349 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ( Rwell ) = ( 4.91e-11 ) ( R ) = ( 1.13e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00372065 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584023 s | Solve Time: 0.253087 s + compositionalMultiphaseFlow: Max pressure change: 7744.838 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.673 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.741943587736273e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.46e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.72e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14462189.383530626 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.62946e+06, 9.9517e+06, 1.09134e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.38239e+06, -421303 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.56879e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.85318e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18347e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.56879e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.73244e+11 } } mol +Time: 1.38e+09 s, dt: 4320000 s, Cycle: 350 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-02 ) ( Rwell ) = ( 4.90e-11 ) ( R ) = ( 1.12e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00375146 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588352 s | Solve Time: 0.252887 s + compositionalMultiphaseFlow: Max pressure change: 7744.607 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.679 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7088017329202074e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.93e-05 ) ( Rwell ) = ( 4.45e-11 ) ( R ) = ( 9.93e-05 ) + Last LinSolve(iter,res) = ( 3, 3.75e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14468715.174604636 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.63597e+06, 9.95857e+06, 1.09195e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.37583e+06, -415199 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57091e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.85637e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18527e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57091e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.75368e+11 } } mol +Time: 1.39e+09 s, dt: 3000000 s, Cycle: 351 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.76e-03 ) ( Rwell ) = ( 4.89e-11 ) ( R ) = ( 7.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00323332 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588716 s | Solve Time: 0.252991 s + compositionalMultiphaseFlow: Max pressure change: 5371.770 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33.106 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.707869053932612e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e-05 ) ( Rwell ) = ( 2.14e-11 ) ( R ) = ( 4.13e-05 ) + Last LinSolve(iter,res) = ( 3, 3.23e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14473244.8681012 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.052 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.64049e+06, 9.96334e+06, 1.09237e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.36927e+06, -409095 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57239e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.85858e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18653e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57239e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.76842e+11 } } mol +Time: 1.39e+09 s, dt: 4320000 s, Cycle: 352 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ( Rwell ) = ( 2.58e-11 ) ( R ) = ( 1.11e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00370675 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585513 s | Solve Time: 0.253087 s + compositionalMultiphaseFlow: Max pressure change: 7750.799 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.590 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.678696046811481e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.56e-05 ) ( Rwell ) = ( 4.44e-11 ) ( R ) = ( 9.56e-05 ) + Last LinSolve(iter,res) = ( 3, 3.71e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14479770.072363568 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.647e+06, 9.97021e+06, 1.09298e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.36472e+06, -404858 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57451e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.86177e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.18833e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57451e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.78966e+11 } } mol +Time: 1.39e+09 s, dt: 4320000 s, Cycle: 353 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ( Rwell ) = ( 4.87e-11 ) ( R ) = ( 1.11e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00372313 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586294 s | Solve Time: 0.25304 s + compositionalMultiphaseFlow: Max pressure change: 7744.324 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.468 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.628381237101962e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.55e-05 ) ( Rwell ) = ( 4.42e-11 ) ( R ) = ( 9.55e-05 ) + Last LinSolve(iter,res) = ( 3, 3.72e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14486294.36714417 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.65351e+06, 9.97708e+06, 1.09359e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.35816e+06, -398755 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57663e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.86495e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19014e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57663e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.8109e+11 } } mol +Time: 1.40e+09 s, dt: 4320000 s, Cycle: 354 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ( Rwell ) = ( 4.86e-11 ) ( R ) = ( 1.11e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00382269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585196 s | Solve Time: 0.252595 s + compositionalMultiphaseFlow: Max pressure change: 7741.645 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.304 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6693802002153433e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.91e-05 ) ( Rwell ) = ( 4.41e-11 ) ( R ) = ( 9.91e-05 ) + Last LinSolve(iter,res) = ( 3, 3.82e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14492816.668413492 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.66002e+06, 9.98394e+06, 1.0942e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.35161e+06, -392651 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.57876e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.86814e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19194e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.57876e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.83214e+11 } } mol +Time: 1.40e+09 s, dt: 4320000 s, Cycle: 355 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-02 ) ( Rwell ) = ( 4.85e-11 ) ( R ) = ( 1.10e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00380455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584807 s | Solve Time: 0.253996 s + compositionalMultiphaseFlow: Max pressure change: 7740.847 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.091 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6431641075852497e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.85e-05 ) ( Rwell ) = ( 4.40e-11 ) ( R ) = ( 9.85e-05 ) + Last LinSolve(iter,res) = ( 3, 3.80e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14499338.20646748 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.66652e+06, 9.9908e+06, 1.09481e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.34505e+06, -386550 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.58088e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.87132e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19375e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.58088e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.85337e+11 } } mol +Time: 1.41e+09 s, dt: 4320000 s, Cycle: 356 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-02 ) ( Rwell ) = ( 4.84e-11 ) ( R ) = ( 1.10e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00379418 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58542 s | Solve Time: 0.253116 s + compositionalMultiphaseFlow: Max pressure change: 7739.775 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.015 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6338995462449333e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.89e-05 ) ( Rwell ) = ( 4.39e-11 ) ( R ) = ( 9.89e-05 ) + Last LinSolve(iter,res) = ( 3, 3.79e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14505858.755959764 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.67303e+06, 9.99767e+06, 1.09542e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.3385e+06, -380449 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.583e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.87451e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19555e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.583e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.87461e+11 } } mol +Time: 1.41e+09 s, dt: 4320000 s, Cycle: 357 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-02 ) ( Rwell ) = ( 4.83e-11 ) ( R ) = ( 1.10e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00373638 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585624 s | Solve Time: 0.253109 s + compositionalMultiphaseFlow: Max pressure change: 7738.599 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.992 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.590870044061333e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.85e-05 ) ( Rwell ) = ( 4.39e-11 ) ( R ) = ( 9.85e-05 ) + Last LinSolve(iter,res) = ( 3, 3.74e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14512378.870697597 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.67953e+06, 1.00045e+07, 1.09603e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.33195e+06, -374348 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.58513e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.87769e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19736e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.58513e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.89584e+11 } } mol +Time: 1.41e+09 s, dt: 4320000 s, Cycle: 358 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-02 ) ( Rwell ) = ( 4.82e-11 ) ( R ) = ( 1.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00374738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583527 s | Solve Time: 0.253246 s + compositionalMultiphaseFlow: Max pressure change: 7737.006 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.937 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5627829836061267e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.84e-05 ) ( Rwell ) = ( 4.38e-11 ) ( R ) = ( 9.84e-05 ) + Last LinSolve(iter,res) = ( 3, 3.75e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14518897.60389747 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.68604e+06, 1.00114e+07, 1.09664e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.32539e+06, -368247 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.58725e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.88088e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19916e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.58725e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.91708e+11 } } mol +Time: 1.42e+09 s, dt: 1320000 s, Cycle: 359 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.33e-03 ) ( Rwell ) = ( 4.81e-11 ) ( R ) = ( 3.33e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00239025 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58352 s | Solve Time: 0.252848 s + compositionalMultiphaseFlow: Max pressure change: 2353.376 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 14.353 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.939638846932162e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.04e-06 ) ( Rwell ) = ( 4.07e-12 ) ( R ) = ( 8.04e-06 ) + Last LinSolve(iter,res) = ( 3, 2.39e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14520888.143594125 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.68802e+06, 1.00135e+07, 1.09683e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.31884e+06, -362148 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.5879e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.88185e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.19971e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.5879e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.92357e+11 } } mol +Time: 1.42e+09 s, dt: 2640000 s, Cycle: 360 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-03 ) ( Rwell ) = ( 8.41e-12 ) ( R ) = ( 6.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0034219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587021 s | Solve Time: 0.252638 s + compositionalMultiphaseFlow: Max pressure change: 4732.373 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 28.697 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4510974935276764e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-05 ) ( Rwell ) = ( 1.63e-11 ) ( R ) = ( 2.56e-05 ) + Last LinSolve(iter,res) = ( 3, 3.42e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14524870.094971934 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.692e+06, 1.00177e+07, 1.0972e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.31684e+06, -360285 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.5892e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.8838e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20082e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.5892e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.93654e+11 } } mol +Time: 1.42e+09 s, dt: 4320000 s, Cycle: 361 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-02 ) ( Rwell ) = ( 2.06e-11 ) ( R ) = ( 1.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00443223 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581949 s | Solve Time: 0.252929 s + compositionalMultiphaseFlow: Max pressure change: 7737.948 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.857 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.4615305620231425e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.04e-05 ) ( Rwell ) = ( 4.36e-11 ) ( R ) = ( 9.04e-05 ) + Last LinSolve(iter,res) = ( 3, 4.43e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14531386.63737235 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.6985e+06, 1.00245e+07, 1.09781e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.31284e+06, -356559 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59132e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.88698e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20262e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59132e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.95778e+11 } } mol +Time: 1.43e+09 s, dt: 4320000 s, Cycle: 362 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-02 ) ( Rwell ) = ( 4.79e-11 ) ( R ) = ( 1.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00379426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584656 s | Solve Time: 0.253683 s + compositionalMultiphaseFlow: Max pressure change: 7732.008 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.770 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5702590522591606e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.96e-05 ) ( Rwell ) = ( 4.35e-11 ) ( R ) = ( 9.96e-05 ) + Last LinSolve(iter,res) = ( 3, 3.79e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14537902.429815233 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.705e+06, 1.00314e+07, 1.09842e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.30629e+06, -350461 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59344e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.89017e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20443e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59344e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 3.97902e+11 } } mol +Time: 1.43e+09 s, dt: 4320000 s, Cycle: 363 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-02 ) ( Rwell ) = ( 4.78e-11 ) ( R ) = ( 1.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0038537 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586746 s | Solve Time: 0.253206 s + compositionalMultiphaseFlow: Max pressure change: 7732.199 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.651 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5407051285064597e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.34e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.85e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14544417.947044013 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.7115e+06, 1.00382e+07, 1.09903e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.29974e+06, -344364 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59557e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.89335e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20623e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59557e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.00025e+11 } } mol +Time: 1.44e+09 s, dt: 4320000 s, Cycle: 364 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ( Rwell ) = ( 4.77e-11 ) ( R ) = ( 1.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.003862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585783 s | Solve Time: 0.253344 s + compositionalMultiphaseFlow: Max pressure change: 7732.856 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.684 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5487675547886113e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.33e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14550932.768137027 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.718e+06, 1.00451e+07, 1.09964e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.2932e+06, -338266 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59769e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.89654e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20804e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59769e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.02149e+11 } } mol +Time: 1.44e+09 s, dt: 4320000 s, Cycle: 365 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ( Rwell ) = ( 4.76e-11 ) ( R ) = ( 1.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00386458 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587356 s | Solve Time: 0.252762 s + compositionalMultiphaseFlow: Max pressure change: 7733.405 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.701 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.522751976208326e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.99e-05 ) ( Rwell ) = ( 4.32e-11 ) ( R ) = ( 9.99e-05 ) + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14557446.754700568 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.72449e+06, 1.00519e+07, 1.10025e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.28665e+06, -332169 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.59982e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.89972e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.20984e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.59982e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.04273e+11 } } mol +Time: 1.44e+09 s, dt: 4320000 s, Cycle: 366 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ( Rwell ) = ( 4.75e-11 ) ( R ) = ( 1.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00392433 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586362 s | Solve Time: 0.252974 s + compositionalMultiphaseFlow: Max pressure change: 7733.527 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.673 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5173931139654826e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-04 ) ( Rwell ) = ( 4.31e-11 ) ( R ) = ( 1.01e-04 ) + Last LinSolve(iter,res) = ( 3, 3.92e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14563959.623143386 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.73099e+06, 1.00588e+07, 1.10086e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.28011e+06, -326072 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60194e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.90291e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.21165e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60194e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.06397e+11 } } mol +Time: 1.45e+09 s, dt: 3000000 s, Cycle: 367 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.47e-03 ) ( Rwell ) = ( 4.74e-11 ) ( R ) = ( 7.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00334398 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587519 s | Solve Time: 0.253178 s + compositionalMultiphaseFlow: Max pressure change: 5364.743 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 32.401 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.454147771060235e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e-05 ) ( Rwell ) = ( 2.07e-11 ) ( R ) = ( 3.96e-05 ) + Last LinSolve(iter,res) = ( 3, 3.34e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14568481.054294683 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.052 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.7355e+06, 1.00635e+07, 1.10128e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.27357e+06, -319976 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60341e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.90512e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2129e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60341e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.07871e+11 } } mol +Time: 1.45e+09 s, dt: 4320000 s, Cycle: 368 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ( Rwell ) = ( 2.50e-11 ) ( R ) = ( 1.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00415769 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585993 s | Solve Time: 0.252956 s + compositionalMultiphaseFlow: Max pressure change: 7738.182 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.520 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.434192635516254e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-04 ) ( Rwell ) = ( 4.30e-11 ) ( R ) = ( 1.03e-04 ) + Last LinSolve(iter,res) = ( 3, 4.16e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14574991.321184102 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.74199e+06, 1.00704e+07, 1.10189e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.26903e+06, -315743 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60554e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.90831e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.21471e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60554e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.09995e+11 } } mol +Time: 1.46e+09 s, dt: 4320000 s, Cycle: 369 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ( Rwell ) = ( 4.73e-11 ) ( R ) = ( 1.08e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00403081 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58717 s | Solve Time: 0.252928 s + compositionalMultiphaseFlow: Max pressure change: 7732.214 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.391 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.528730046469363e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.49e-05 ) ( Rwell ) = ( 4.29e-11 ) ( R ) = ( 9.49e-05 ) + Last LinSolve(iter,res) = ( 3, 4.03e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14581500.98883982 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.74849e+06, 1.00772e+07, 1.1025e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.26249e+06, -309649 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60766e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.91149e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.21651e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60766e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.12118e+11 } } mol +Time: 1.46e+09 s, dt: 4320000 s, Cycle: 370 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ( Rwell ) = ( 4.72e-11 ) ( R ) = ( 1.07e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0040425 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581822 s | Solve Time: 0.253232 s + compositionalMultiphaseFlow: Max pressure change: 7733.039 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.430 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5136547643356266e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.50e-05 ) ( Rwell ) = ( 4.28e-11 ) ( R ) = ( 9.50e-05 ) + Last LinSolve(iter,res) = ( 3, 4.04e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14588009.126878569 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.75498e+06, 1.00841e+07, 1.10311e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.25596e+06, -303555 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.60978e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.91468e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.21832e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.60978e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.14241e+11 } } mol +Time: 1.46e+09 s, dt: 4320000 s, Cycle: 371 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ( Rwell ) = ( 4.71e-11 ) ( R ) = ( 1.07e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00404872 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583082 s | Solve Time: 0.253011 s + compositionalMultiphaseFlow: Max pressure change: 7733.217 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.440 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4925513752993567e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.49e-05 ) ( Rwell ) = ( 4.27e-11 ) ( R ) = ( 9.49e-05 ) + Last LinSolve(iter,res) = ( 3, 4.05e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14594516.350047965 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.76147e+06, 1.00909e+07, 1.10372e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.24942e+06, -297462 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61191e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.91786e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22012e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61191e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.16365e+11 } } mol +Time: 1.47e+09 s, dt: 4320000 s, Cycle: 372 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ( Rwell ) = ( 4.70e-11 ) ( R ) = ( 1.07e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0040547 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585009 s | Solve Time: 0.253074 s + compositionalMultiphaseFlow: Max pressure change: 7733.174 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.405 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.45977041846146e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.48e-05 ) ( Rwell ) = ( 4.26e-11 ) ( R ) = ( 9.48e-05 ) + Last LinSolve(iter,res) = ( 3, 4.05e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14601022.687093843 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.76796e+06, 1.00977e+07, 1.10433e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.24289e+06, -291370 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61403e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.92105e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22193e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61403e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.18488e+11 } } mol +Time: 1.47e+09 s, dt: 4320000 s, Cycle: 373 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 4.69e-11 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00406401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585537 s | Solve Time: 0.253078 s + compositionalMultiphaseFlow: Max pressure change: 7732.955 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.327 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.451000600256492e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.47e-05 ) ( Rwell ) = ( 4.25e-11 ) ( R ) = ( 9.47e-05 ) + Last LinSolve(iter,res) = ( 3, 4.06e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14607528.123874556 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.77445e+06, 1.01046e+07, 1.10494e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.23636e+06, -285279 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61615e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.92423e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22373e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61615e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.20611e+11 } } mol +Time: 1.48e+09 s, dt: 4320000 s, Cycle: 374 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 4.68e-11 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00388891 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585375 s | Solve Time: 0.253146 s + compositionalMultiphaseFlow: Max pressure change: 7733.283 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.199 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.423992294664501e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-04 ) ( Rwell ) = ( 4.24e-11 ) ( R ) = ( 1.05e-04 ) + Last LinSolve(iter,res) = ( 3, 3.89e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14614034.287407972 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.78093e+06, 1.01114e+07, 1.10555e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.22983e+06, -279188 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61828e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.92742e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22554e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61828e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.22735e+11 } } mol +Time: 1.48e+09 s, dt: 1320000 s, Cycle: 375 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-03 ) ( Rwell ) = ( 4.67e-11 ) ( R ) = ( 3.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00251076 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583325 s | Solve Time: 0.253311 s + compositionalMultiphaseFlow: Max pressure change: 2352.339 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 14.115 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.660815685595068e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.70e-06 ) ( Rwell ) = ( 3.95e-12 ) ( R ) = ( 6.70e-06 ) + Last LinSolve(iter,res) = ( 3, 2.51e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14616021.518392963 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.78292e+06, 1.01135e+07, 1.10574e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.2233e+06, -273095 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.61893e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.92839e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22609e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.61893e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.23383e+11 } } mol +Time: 1.48e+09 s, dt: 2640000 s, Cycle: 376 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.46e-03 ) ( Rwell ) = ( 8.22e-12 ) ( R ) = ( 6.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00317764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586643 s | Solve Time: 0.252794 s + compositionalMultiphaseFlow: Max pressure change: 4729.183 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 28.149 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3562306020741275e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-05 ) ( Rwell ) = ( 1.58e-11 ) ( R ) = ( 2.77e-05 ) + Last LinSolve(iter,res) = ( 3, 3.18e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14619995.35689799 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.78688e+06, 1.01177e+07, 1.10611e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.2213e+06, -271235 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62022e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.93034e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.22719e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62022e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.24681e+11 } } mol +Time: 1.49e+09 s, dt: 4320000 s, Cycle: 377 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 2.01e-11 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00388931 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582236 s | Solve Time: 0.253039 s + compositionalMultiphaseFlow: Max pressure change: 7737.307 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.011 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.22652365375631e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-04 ) ( Rwell ) = ( 4.23e-11 ) ( R ) = ( 1.04e-04 ) + Last LinSolve(iter,res) = ( 3, 3.89e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14626499.383616328 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.79337e+06, 1.01245e+07, 1.10672e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.21731e+06, -267513 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62235e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.93352e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.229e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62235e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.26804e+11 } } mol +Time: 1.49e+09 s, dt: 4320000 s, Cycle: 378 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 4.65e-11 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00436816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590905 s | Solve Time: 0.253225 s + compositionalMultiphaseFlow: Max pressure change: 7731.660 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.979 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4870699910639615e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.72e-05 ) ( Rwell ) = ( 4.21e-11 ) ( R ) = ( 9.72e-05 ) + Last LinSolve(iter,res) = ( 3, 4.37e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14633002.138666593 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.79985e+06, 1.01313e+07, 1.10733e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.21079e+06, -261423 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62447e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.93671e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2308e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62447e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.28928e+11 } } mol +Time: 1.49e+09 s, dt: 4320000 s, Cycle: 379 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 4.64e-11 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00438335 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582365 s | Solve Time: 0.253832 s + compositionalMultiphaseFlow: Max pressure change: 7731.610 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.956 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.415462595495299e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.78e-05 ) ( Rwell ) = ( 4.20e-11 ) ( R ) = ( 9.78e-05 ) + Last LinSolve(iter,res) = ( 3, 4.38e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14639504.105704144 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.80634e+06, 1.01382e+07, 1.10793e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.20426e+06, -255333 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62659e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.93989e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23261e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62659e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.31052e+11 } } mol +Time: 1.50e+09 s, dt: 4320000 s, Cycle: 380 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 4.63e-11 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00440265 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585189 s | Solve Time: 0.25299 s + compositionalMultiphaseFlow: Max pressure change: 7730.833 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.921 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.788366361139438e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.91e-05 ) ( Rwell ) = ( 4.20e-11 ) ( R ) = ( 9.91e-05 ) + Last LinSolve(iter,res) = ( 3, 4.40e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14646005.2688165 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.81282e+06, 1.0145e+07, 1.10854e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.19773e+06, -249244 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.62872e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.94308e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23441e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.62872e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.33175e+11 } } mol +Time: 1.50e+09 s, dt: 4320000 s, Cycle: 381 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 4.62e-11 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00418816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586085 s | Solve Time: 0.253135 s + compositionalMultiphaseFlow: Max pressure change: 7728.136 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.968 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9310958682415844e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.73e-05 ) ( Rwell ) = ( 4.19e-11 ) ( R ) = ( 8.73e-05 ) + Last LinSolve(iter,res) = ( 3, 4.19e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14652505.51423642 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.81931e+06, 1.01518e+07, 1.10915e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.1912e+06, -243155 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63084e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.94626e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23622e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63084e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.35299e+11 } } mol +Time: 1.51e+09 s, dt: 4320000 s, Cycle: 382 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.61e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00439788 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58359 s | Solve Time: 0.253215 s + compositionalMultiphaseFlow: Max pressure change: 7726.695 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.927 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.437276668265653e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.18e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 4.40e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14659004.11860391 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.82579e+06, 1.01586e+07, 1.10976e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.18468e+06, -237067 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63296e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.94945e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23802e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63296e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.37422e+11 } } mol +Time: 1.51e+09 s, dt: 3000000 s, Cycle: 383 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.25e-03 ) ( Rwell ) = ( 4.60e-11 ) ( R ) = ( 7.25e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00341679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585993 s | Solve Time: 0.253127 s + compositionalMultiphaseFlow: Max pressure change: 5359.039 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 31.896 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.282819685008654e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-05 ) ( Rwell ) = ( 2.01e-11 ) ( R ) = ( 3.59e-05 ) + Last LinSolve(iter,res) = ( 3, 3.42e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14663516.807602791 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.83029e+06, 1.01634e+07, 1.11018e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.17816e+06, -230980 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63444e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.95166e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.23927e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63444e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.38897e+11 } } mol +Time: 1.51e+09 s, dt: 4320000 s, Cycle: 384 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 2.43e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00440519 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58787 s | Solve Time: 0.252637 s + compositionalMultiphaseFlow: Max pressure change: 7729.737 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.828 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.271798811128491e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-04 ) ( Rwell ) = ( 4.16e-11 ) ( R ) = ( 1.00e-04 ) + Last LinSolve(iter,res) = ( 3, 4.41e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14670014.181678811 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.83677e+06, 1.01702e+07, 1.11079e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.17363e+06, -226753 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63656e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.95485e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24108e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63656e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.4102e+11 } } mol +Time: 1.52e+09 s, dt: 4320000 s, Cycle: 385 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.59e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00447666 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582235 s | Solve Time: 0.253048 s + compositionalMultiphaseFlow: Max pressure change: 7720.955 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.811 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3643201096934519e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-04 ) ( Rwell ) = ( 4.15e-11 ) ( R ) = ( 1.02e-04 ) + Last LinSolve(iter,res) = ( 3, 4.48e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14676510.481824405 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.84324e+06, 1.0177e+07, 1.1114e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.1671e+06, -220666 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.63869e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.95803e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24288e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.63869e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.43143e+11 } } mol +Time: 1.52e+09 s, dt: 4320000 s, Cycle: 386 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.58e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00449089 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584826 s | Solve Time: 0.252906 s + compositionalMultiphaseFlow: Max pressure change: 7722.308 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.803 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3891058786862374e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-04 ) ( Rwell ) = ( 4.14e-11 ) ( R ) = ( 1.02e-04 ) + Last LinSolve(iter,res) = ( 3, 4.49e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14683006.062725583 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.84972e+06, 1.01838e+07, 1.11201e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.16059e+06, -214581 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64081e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.96122e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24469e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64081e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.45267e+11 } } mol +Time: 1.53e+09 s, dt: 4320000 s, Cycle: 387 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.57e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00413933 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582451 s | Solve Time: 0.252979 s + compositionalMultiphaseFlow: Max pressure change: 7725.273 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.835 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4205302506796755e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.44e-05 ) ( Rwell ) = ( 4.14e-11 ) ( R ) = ( 9.44e-05 ) + Last LinSolve(iter,res) = ( 3, 4.14e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14689502.602426903 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.8562e+06, 1.01906e+07, 1.11262e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.15407e+06, -208496 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64293e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9644e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.24649e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64293e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.4739e+11 } } mol +Time: 1.53e+09 s, dt: 4320000 s, Cycle: 388 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.56e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00426817 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584745 s | Solve Time: 0.252858 s + compositionalMultiphaseFlow: Max pressure change: 7723.649 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.822 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3715157437820267e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.00e-05 ) ( Rwell ) = ( 4.13e-11 ) ( R ) = ( 9.00e-05 ) + Last LinSolve(iter,res) = ( 3, 4.27e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14695997.194650361 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.86267e+06, 1.01975e+07, 1.11323e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.14755e+06, -202409 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64506e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.96759e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2483e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64506e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.49514e+11 } } mol +Time: 1.54e+09 s, dt: 4320000 s, Cycle: 389 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.55e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00415572 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582978 s | Solve Time: 0.254028 s + compositionalMultiphaseFlow: Max pressure change: 7726.467 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.764 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3807805060727105e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.46e-05 ) ( Rwell ) = ( 4.12e-11 ) ( R ) = ( 9.46e-05 ) + Last LinSolve(iter,res) = ( 3, 4.16e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14702491.199968915 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.86915e+06, 1.02043e+07, 1.11384e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.14103e+06, -196324 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64718e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.97077e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.2501e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64718e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.51637e+11 } } mol +Time: 1.54e+09 s, dt: 4320000 s, Cycle: 390 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 4.54e-11 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00398121 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586448 s | Solve Time: 0.252998 s + compositionalMultiphaseFlow: Max pressure change: 7724.530 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.734 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4463382541917156e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.92e-05 ) ( Rwell ) = ( 4.11e-11 ) ( R ) = ( 9.92e-05 ) + Last LinSolve(iter,res) = ( 3, 3.98e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14708983.820481012 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.87562e+06, 1.02111e+07, 1.11444e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.13451e+06, -190240 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.6493e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.97396e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25191e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.6493e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.53761e+11 } } mol +Time: 1.55e+09 s, dt: 1320000 s, Cycle: 391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-03 ) ( Rwell ) = ( 4.53e-11 ) ( R ) = ( 3.16e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00261736 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583427 s | Solve Time: 0.252875 s + compositionalMultiphaseFlow: Max pressure change: 2351.723 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13.976 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.423050715660295e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.49e-06 ) ( Rwell ) = ( 3.83e-12 ) ( R ) = ( 7.49e-06 ) + Last LinSolve(iter,res) = ( 3, 2.62e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14710967.603001034 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.022 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.87759e+06, 1.02132e+07, 1.11463e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.128e+06, -184156 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.64995e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.97493e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25246e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.64995e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.54409e+11 } } mol +Time: 1.55e+09 s, dt: 2640000 s, Cycle: 392 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.31e-03 ) ( Rwell ) = ( 8.04e-12 ) ( R ) = ( 6.31e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00317318 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586634 s | Solve Time: 0.252805 s + compositionalMultiphaseFlow: Max pressure change: 4724.970 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.927 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2870277279762874e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-05 ) ( Rwell ) = ( 1.53e-11 ) ( R ) = ( 2.67e-05 ) + Last LinSolve(iter,res) = ( 3, 3.17e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14714933.87745844 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.88155e+06, 1.02173e+07, 1.115e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.12601e+06, -182297 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65125e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.97688e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25356e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65125e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.55707e+11 } } mol +Time: 1.55e+09 s, dt: 4320000 s, Cycle: 393 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 1.95e-11 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00402975 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58809 s | Solve Time: 0.252906 s + compositionalMultiphaseFlow: Max pressure change: 7733.208 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.791 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.112854073008322e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.66e-05 ) ( Rwell ) = ( 4.10e-11 ) ( R ) = ( 9.66e-05 ) + Last LinSolve(iter,res) = ( 3, 4.03e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14721426.027905297 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.88802e+06, 1.02241e+07, 1.11561e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.12203e+06, -178580 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65337e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.98006e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25537e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65337e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.57831e+11 } } mol +Time: 1.55e+09 s, dt: 4320000 s, Cycle: 394 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 4.52e-11 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00404391 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584541 s | Solve Time: 0.252813 s + compositionalMultiphaseFlow: Max pressure change: 7728.452 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.858 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3689048278541236e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.69e-05 ) ( Rwell ) = ( 4.09e-11 ) ( R ) = ( 9.69e-05 ) + Last LinSolve(iter,res) = ( 3, 4.04e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14727917.671140127 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.89449e+06, 1.02309e+07, 1.11622e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.11552e+06, -172497 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.6555e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.98325e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25717e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.6555e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.59955e+11 } } mol +Time: 1.56e+09 s, dt: 4320000 s, Cycle: 395 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 4.51e-11 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00391148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584749 s | Solve Time: 0.253047 s + compositionalMultiphaseFlow: Max pressure change: 7727.495 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.883 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3767074541769517e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.55e-05 ) ( Rwell ) = ( 4.08e-11 ) ( R ) = ( 9.55e-05 ) + Last LinSolve(iter,res) = ( 3, 3.91e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14734407.805856543 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.90096e+06, 1.02378e+07, 1.11683e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.109e+06, -166413 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65762e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.98643e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.25898e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65762e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.62078e+11 } } mol +Time: 1.56e+09 s, dt: 4320000 s, Cycle: 396 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 4.50e-11 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00420473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586794 s | Solve Time: 0.25276 s + compositionalMultiphaseFlow: Max pressure change: 7726.366 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.944 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5262057679054095e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.38e-05 ) ( Rwell ) = ( 4.07e-11 ) ( R ) = ( 9.38e-05 ) + Last LinSolve(iter,res) = ( 3, 4.20e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14740895.978817716 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.90743e+06, 1.02446e+07, 1.11743e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.10249e+06, -160331 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.65974e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.98962e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26078e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.65974e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.64202e+11 } } mol +Time: 1.57e+09 s, dt: 4320000 s, Cycle: 397 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 4.49e-11 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00421225 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588704 s | Solve Time: 0.253705 s + compositionalMultiphaseFlow: Max pressure change: 7726.544 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.991 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.385072166433133e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.40e-05 ) ( Rwell ) = ( 4.06e-11 ) ( R ) = ( 9.40e-05 ) + Last LinSolve(iter,res) = ( 3, 4.21e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14747383.25569581 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9139e+06, 1.02514e+07, 1.11804e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.09598e+06, -154250 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66187e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9928e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26259e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66187e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.66325e+11 } } mol +Time: 1.57e+09 s, dt: 4320000 s, Cycle: 398 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 4.48e-11 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.004183 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584756 s | Solve Time: 0.253166 s + compositionalMultiphaseFlow: Max pressure change: 7727.189 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.998 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3613530697463858e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.48e-05 ) ( Rwell ) = ( 4.05e-11 ) ( R ) = ( 9.48e-05 ) + Last LinSolve(iter,res) = ( 3, 4.18e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14753870.164189477 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.92037e+06, 1.02582e+07, 1.11865e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08947e+06, -148170 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66399e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99599e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26439e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66399e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.68448e+11 } } mol +Time: 1.58e+09 s, dt: 3000000 s, Cycle: 399 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.09e-03 ) ( Rwell ) = ( 4.47e-11 ) ( R ) = ( 7.09e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00343397 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583679 s | Solve Time: 0.253414 s + compositionalMultiphaseFlow: Max pressure change: 5361.001 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 31.943 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.259017525765074e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.92e-05 ) ( Rwell ) = ( 1.95e-11 ) ( R ) = ( 3.92e-05 ) + Last LinSolve(iter,res) = ( 3, 3.43e-03 ) +wellControls1: well is shut +wellControls2: BHP (at the specified reference elevation): 14758374.420722693 Pa +wellControls2: Total rate: 491.57792280869756 mol/s; total surface volumetric rate: 11.57407407407407 sm3/s +wellControls2: Phase 0 surface volumetric rate: 0 sm3/s +wellControls2: Phase 1 surface volumetric rate: 11.57407407407407 sm3/s +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.92486e+06, 1.02629e+07, 1.11907e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08296e+06, -142090 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.58e+09 s, dt: 4320000 s, Cycle: 400 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.77e+01 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.77e+01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0022691 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588567 s | Solve Time: 0.376487 s + compositionalMultiphaseFlow: Max pressure change: 823587.410 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 380.672 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0010510145168609597 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.31e+00 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.31e+00 ) + Last LinSolve(iter,res) = ( 3, 2.27e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00478164 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582721 s | Solve Time: 0.174037 s + compositionalMultiphaseFlow: Max pressure change: 53442.394 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 92.863 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0019420390449796932 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.87e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.87e-02 ) + Last LinSolve(iter,res) = ( 2, 4.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00444178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589219 s | Solve Time: 0.252777 s + compositionalMultiphaseFlow: Max pressure change: 421.019 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 7.465 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 0.0019418271842204238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.15e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.15e-05 ) + Last LinSolve(iter,res) = ( 3, 4.44e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 7.841 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Time-step required will be increased based on state change. +compflowStatistics, Region1: Pressure (min, average, max): 9.93084e+06, 1.02632e+07, 1.06446e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07845e+06, -137868 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.58e+09 s, dt: 4320000 s, Cycle: 401 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-01 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-01 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00426831 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585356 s | Solve Time: 0.332437 s + compositionalMultiphaseFlow: Max pressure change: 15261.665 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 121.903 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.6266954908124056e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.22e-03 ) + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00396267 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58384 s | Solve Time: 0.253381 s + compositionalMultiphaseFlow: Max pressure change: 19.655 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 4.839 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.622972921270897e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-06 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.41e-06 ) + Last LinSolve(iter,res) = ( 3, 3.96e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.148 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.93596e+06, 1.02634e+07, 1.06476e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07283e+06, -900225 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.59e+09 s, dt: 4320000 s, Cycle: 402 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.82e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.82e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0069072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583189 s | Solve Time: 0.252716 s + compositionalMultiphaseFlow: Max pressure change: 4683.457 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 115.878 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.072482098344988e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.03e-04 ) + Last LinSolve(iter,res) = ( 3, 6.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.94012e+06, 1.02635e+07, 1.0649e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07751e+06, -898284 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.59e+09 s, dt: 4320000 s, Cycle: 403 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.74e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0037454 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587085 s | Solve Time: 0.252774 s + compositionalMultiphaseFlow: Max pressure change: 3353.666 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 109.325 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.341213188349904e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.27e-04 ) + Last LinSolve(iter,res) = ( 3, 3.75e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.94343e+06, 1.02636e+07, 1.06493e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08019e+06, -897628 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.60e+09 s, dt: 4320000 s, Cycle: 404 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.59e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.59e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0027004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583578 s | Solve Time: 0.253384 s + compositionalMultiphaseFlow: Max pressure change: 2659.723 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 102.658 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.594694542005897e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.64e-05 ) + Last LinSolve(iter,res) = ( 3, 2.70e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.94606e+06, 1.02637e+07, 1.06491e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08155e+06, -897729 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.60e+09 s, dt: 4320000 s, Cycle: 405 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.45e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.45e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00197546 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586538 s | Solve Time: 0.252906 s + compositionalMultiphaseFlow: Max pressure change: 2129.681 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 96.208 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.602247138525307e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.23e-04 ) + Last LinSolve(iter,res) = ( 3, 1.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.94818e+06, 1.02638e+07, 1.06487e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0822e+06, -898186 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69922e+11 } } mol +Time: 1.60e+09 s, dt: 4320000 s, Cycle: 406 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.32e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.32e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00184766 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586656 s | Solve Time: 0.25272 s + compositionalMultiphaseFlow: Max pressure change: 1732.515 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 90.749 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.719659788321451e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.24e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.24e-05 ) + Last LinSolve(iter,res) = ( 3, 1.85e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.017 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9499e+06, 1.02639e+07, 1.06482e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08244e+06, -898793 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69922e+11 } } mol +Time: 1.61e+09 s, dt: 1320000 s, Cycle: 407 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00333378 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583633 s | Solve Time: 0.173678 s + compositionalMultiphaseFlow: Max pressure change: 497.008 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.388 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7619760692987327e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-05 ) + Last LinSolve(iter,res) = ( 2, 3.33e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9504e+06, 1.02639e+07, 1.0648e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08245e+06, -899438 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69922e+11 } } mol +Time: 1.61e+09 s, dt: 2640000 s, Cycle: 408 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.32e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0062848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58735 s | Solve Time: 0.174257 s + compositionalMultiphaseFlow: Max pressure change: 883.618 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.456 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.667711608871919e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 4.38e-05 ) + Last LinSolve(iter,res) = ( 2, 6.28e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95128e+06, 1.0264e+07, 1.06477e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08245e+06, -899648 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.61e+09 s, dt: 4320000 s, Cycle: 409 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.09e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00969486 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582734 s | Solve Time: 0.173991 s + compositionalMultiphaseFlow: Max pressure change: 1218.832 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 83.814 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5807374079468417e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.21e-04 ) + Last LinSolve(iter,res) = ( 2, 9.69e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9525e+06, 1.02641e+07, 1.06472e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08236e+06, -900032 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66547e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69923e+11 } } mol +Time: 1.62e+09 s, dt: 4320000 s, Cycle: 410 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00969649 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586219 s | Solve Time: 0.174255 s + compositionalMultiphaseFlow: Max pressure change: 1042.157 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 81.712 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.885629580395843e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.25e-04 ) + Last LinSolve(iter,res) = ( 2, 9.70e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.010 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95354e+06, 1.02641e+07, 1.06468e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08232e+06, -900618 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26565e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69924e+11 } } mol +Time: 1.62e+09 s, dt: 4320000 s, Cycle: 411 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.95e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00963492 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587033 s | Solve Time: 0.173992 s + compositionalMultiphaseFlow: Max pressure change: 905.257 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 79.432 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.542951614947775e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.27e-04 ) + Last LinSolve(iter,res) = ( 2, 9.63e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95444e+06, 1.02642e+07, 1.06464e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08224e+06, -901150 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69924e+11 } } mol +Time: 1.63e+09 s, dt: 4320000 s, Cycle: 412 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.90e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00946075 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583025 s | Solve Time: 0.174006 s + compositionalMultiphaseFlow: Max pressure change: 786.960 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 76.943 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.218453232782913e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.27e-04 ) + Last LinSolve(iter,res) = ( 2, 9.46e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.008 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95523e+06, 1.02643e+07, 1.06461e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08211e+06, -901616 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69925e+11 } } mol +Time: 1.63e+09 s, dt: 4320000 s, Cycle: 413 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.85e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00934233 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584338 s | Solve Time: 0.174139 s + compositionalMultiphaseFlow: Max pressure change: 694.084 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 74.319 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9279917784498224e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.28e-04 ) + Last LinSolve(iter,res) = ( 2, 9.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.007 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95592e+06, 1.02643e+07, 1.06459e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08195e+06, -902019 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69925e+11 } } mol +Time: 1.63e+09 s, dt: 4320000 s, Cycle: 414 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00923395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585595 s | Solve Time: 0.174221 s + compositionalMultiphaseFlow: Max pressure change: 616.802 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 71.594 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7518023820439765e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.29e-04 ) + Last LinSolve(iter,res) = ( 2, 9.23e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95654e+06, 1.02644e+07, 1.06457e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08177e+06, -902365 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69925e+11 } } mol +Time: 1.64e+09 s, dt: 3000000 s, Cycle: 415 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.21e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00617325 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585703 s | Solve Time: 0.174431 s + compositionalMultiphaseFlow: Max pressure change: 395.799 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 48.344 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0030281359263427e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.15e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.15e-05 ) + Last LinSolve(iter,res) = ( 2, 6.17e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95694e+06, 1.02644e+07, 1.06456e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08158e+06, -902659 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69926e+11 } } mol +Time: 1.64e+09 s, dt: 4320000 s, Cycle: 416 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.70e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00904849 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582347 s | Solve Time: 0.174075 s + compositionalMultiphaseFlow: Max pressure change: 511.389 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 66.842 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.98211373331803e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.26e-04 ) + Last LinSolve(iter,res) = ( 2, 9.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95745e+06, 1.02645e+07, 1.06455e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08146e+06, -902846 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69926e+11 } } mol +Time: 1.65e+09 s, dt: 4320000 s, Cycle: 417 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.64e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00900558 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585275 s | Solve Time: 0.17388 s + compositionalMultiphaseFlow: Max pressure change: 467.264 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 64.842 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3740097433156961e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.25e-04 ) + Last LinSolve(iter,res) = ( 2, 9.01e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95791e+06, 1.02645e+07, 1.06455e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08124e+06, -903058 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69926e+11 } } mol +Time: 1.65e+09 s, dt: 4320000 s, Cycle: 418 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00864972 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582997 s | Solve Time: 0.180968 s + compositionalMultiphaseFlow: Max pressure change: 437.772 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 63.414 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3275134419510337e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.24e-04 ) + Last LinSolve(iter,res) = ( 2, 8.65e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95833e+06, 1.02646e+07, 1.06455e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08104e+06, -903239 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69927e+11 } } mol +Time: 1.65e+09 s, dt: 4320000 s, Cycle: 419 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.53e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00863772 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588761 s | Solve Time: 0.176888 s + compositionalMultiphaseFlow: Max pressure change: 415.390 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 62.066 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2347922463407102e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.22e-04 ) + Last LinSolve(iter,res) = ( 2, 8.64e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95872e+06, 1.02646e+07, 1.06456e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08082e+06, -903387 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69927e+11 } } mol +Time: 1.66e+09 s, dt: 4320000 s, Cycle: 420 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00861903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585322 s | Solve Time: 0.175067 s + compositionalMultiphaseFlow: Max pressure change: 395.694 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 60.737 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.148166695719155e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.21e-04 ) + Last LinSolve(iter,res) = ( 2, 8.62e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95907e+06, 1.02647e+07, 1.06456e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08061e+06, -903509 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69927e+11 } } mol +Time: 1.66e+09 s, dt: 4320000 s, Cycle: 421 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00853828 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583088 s | Solve Time: 0.174137 s + compositionalMultiphaseFlow: Max pressure change: 380.569 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 59.320 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0627481616953816e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 2, 8.54e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95939e+06, 1.02648e+07, 1.06457e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08039e+06, -903494 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69927e+11 } } mol +Time: 1.67e+09 s, dt: 4320000 s, Cycle: 422 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.44e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00861699 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586474 s | Solve Time: 0.173926 s + compositionalMultiphaseFlow: Max pressure change: 366.893 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 57.824 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.800757928557502e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 2, 8.62e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9597e+06, 1.02648e+07, 1.06459e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.08017e+06, -903455 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69927e+11 } } mol +Time: 1.67e+09 s, dt: 1320000 s, Cycle: 423 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 4.31e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00261817 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.581934 s | Solve Time: 0.17402 s + compositionalMultiphaseFlow: Max pressure change: 113.077 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 17.531 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0871667641465521e-05 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.92e-06 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.92e-06 ) + Last LinSolve(iter,res) = ( 2, 2.62e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95979e+06, 1.02648e+07, 1.06459e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07994e+06, -903400 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69927e+11 } } mol +Time: 1.67e+09 s, dt: 2640000 s, Cycle: 424 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.59e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00513162 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582382 s | Solve Time: 0.174461 s + compositionalMultiphaseFlow: Max pressure change: 216.734 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.494 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.1302437811797645e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 4.26e-05 ) + Last LinSolve(iter,res) = ( 2, 5.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.95996e+06, 1.02649e+07, 1.0646e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07989e+06, -903394 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.68e+09 s, dt: 4320000 s, Cycle: 425 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.38e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00845325 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585208 s | Solve Time: 0.174888 s + compositionalMultiphaseFlow: Max pressure change: 343.121 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 54.831 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.535923468553584e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.15e-04 ) + Last LinSolve(iter,res) = ( 2, 8.45e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96023e+06, 1.02649e+07, 1.06461e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07974e+06, -903346 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.68e+09 s, dt: 4320000 s, Cycle: 426 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.35e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00858134 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585786 s | Solve Time: 0.174381 s + compositionalMultiphaseFlow: Max pressure change: 335.673 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 53.202 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 7.358757831976703e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 2, 8.58e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96048e+06, 1.0265e+07, 1.06463e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07951e+06, -903264 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.68e+09 s, dt: 4320000 s, Cycle: 427 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.31e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00855886 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585393 s | Solve Time: 0.174178 s + compositionalMultiphaseFlow: Max pressure change: 327.826 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 52.379 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.904216564018739e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.13e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.13e-04 ) + Last LinSolve(iter,res) = ( 2, 8.56e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96072e+06, 1.0265e+07, 1.06465e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07928e+06, -903180 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.69e+09 s, dt: 4320000 s, Cycle: 428 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.28e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0085612 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584502 s | Solve Time: 0.174191 s + compositionalMultiphaseFlow: Max pressure change: 321.794 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 51.563 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.493997414258601e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.14e-04 ) + Last LinSolve(iter,res) = ( 2, 8.56e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96095e+06, 1.02651e+07, 1.06467e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07905e+06, -903089 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.69e+09 s, dt: 4320000 s, Cycle: 429 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.24e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00855953 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587092 s | Solve Time: 0.174029 s + compositionalMultiphaseFlow: Max pressure change: 316.553 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 50.665 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 6.170769750735161e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.15e-04 ) + Last LinSolve(iter,res) = ( 2, 8.56e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96116e+06, 1.02651e+07, 1.06469e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07882e+06, -902993 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.70e+09 s, dt: 4320000 s, Cycle: 430 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.23e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00865048 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58453 s | Solve Time: 0.173944 s + compositionalMultiphaseFlow: Max pressure change: 311.674 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 49.695 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.864782902653687e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 2, 8.65e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96137e+06, 1.02652e+07, 1.06472e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07859e+06, -902893 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.70e+09 s, dt: 3000000 s, Cycle: 431 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00604443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586707 s | Solve Time: 0.175022 s + compositionalMultiphaseFlow: Max pressure change: 216.991 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.014 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.709182368278775e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.25e-05 ) + Last LinSolve(iter,res) = ( 2, 6.04e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96151e+06, 1.02652e+07, 1.06473e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07836e+06, -902792 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69928e+11 } } mol +Time: 1.70e+09 s, dt: 4320000 s, Cycle: 432 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.19e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00851753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588609 s | Solve Time: 0.174413 s + compositionalMultiphaseFlow: Max pressure change: 304.542 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 47.923 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.029603511312985e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 2, 8.52e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96171e+06, 1.02652e+07, 1.06475e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0782e+06, -902726 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69929e+11 } } mol +Time: 1.71e+09 s, dt: 4320000 s, Cycle: 433 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00846368 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590489 s | Solve Time: 0.174276 s + compositionalMultiphaseFlow: Max pressure change: 303.251 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 46.801 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.062106206432659e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.14e-04 ) + Last LinSolve(iter,res) = ( 2, 8.46e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9619e+06, 1.02653e+07, 1.06478e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07796e+06, -902618 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69929e+11 } } mol +Time: 1.71e+09 s, dt: 4320000 s, Cycle: 434 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.15e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0084786 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58772 s | Solve Time: 0.17396 s + compositionalMultiphaseFlow: Max pressure change: 300.768 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 45.639 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.811703661067313e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.15e-04 ) + Last LinSolve(iter,res) = ( 2, 8.48e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96208e+06, 1.02653e+07, 1.0648e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07773e+06, -902516 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69929e+11 } } mol +Time: 1.72e+09 s, dt: 4320000 s, Cycle: 435 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.12e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00847644 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586873 s | Solve Time: 0.174353 s + compositionalMultiphaseFlow: Max pressure change: 298.409 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 44.443 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5147599636585767e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.16e-04 ) + Last LinSolve(iter,res) = ( 2, 8.48e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96226e+06, 1.02654e+07, 1.06483e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0775e+06, -902416 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19554e+12, 4.69929e+11 } } mol +Time: 1.72e+09 s, dt: 4320000 s, Cycle: 436 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.10e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00847019 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585794 s | Solve Time: 0.174119 s + compositionalMultiphaseFlow: Max pressure change: 296.376 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.292 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.226393810480289e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.16e-04 ) + Last LinSolve(iter,res) = ( 2, 8.47e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96244e+06, 1.02654e+07, 1.06486e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07726e+06, -902317 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.73e+09 s, dt: 4320000 s, Cycle: 437 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.07e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00838722 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584482 s | Solve Time: 0.174383 s + compositionalMultiphaseFlow: Max pressure change: 297.834 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.822 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.940962993720376e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.17e-04 ) + Last LinSolve(iter,res) = ( 2, 8.39e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96262e+06, 1.02655e+07, 1.06488e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07703e+06, -902220 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.73e+09 s, dt: 4320000 s, Cycle: 438 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00844924 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585963 s | Solve Time: 0.174151 s + compositionalMultiphaseFlow: Max pressure change: 301.230 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.347 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7836715016670297e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.18e-04 ) + Last LinSolve(iter,res) = ( 2, 8.45e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96279e+06, 1.02655e+07, 1.06491e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07679e+06, -902125 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.73e+09 s, dt: 1320000 s, Cycle: 439 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.13e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.13e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00256979 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586321 s | Solve Time: 0.174032 s + compositionalMultiphaseFlow: Max pressure change: 92.045 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.851 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.83825257283177e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.00e-06 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.00e-06 ) + Last LinSolve(iter,res) = ( 2, 2.57e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96284e+06, 1.02655e+07, 1.06492e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07656e+06, -902034 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.74e+09 s, dt: 2640000 s, Cycle: 440 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.24e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00510105 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584598 s | Solve Time: 0.174386 s + compositionalMultiphaseFlow: Max pressure change: 185.218 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25.549 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7373450812430136e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 4.43e-05 ) + Last LinSolve(iter,res) = ( 2, 5.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96294e+06, 1.02655e+07, 1.06493e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0765e+06, -902019 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.74e+09 s, dt: 4320000 s, Cycle: 441 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00832527 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588785 s | Solve Time: 0.173781 s + compositionalMultiphaseFlow: Max pressure change: 308.587 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.309 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7460625003093995e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.19e-04 ) + Last LinSolve(iter,res) = ( 2, 8.33e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9631e+06, 1.02656e+07, 1.06496e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07635e+06, -901957 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.74e+09 s, dt: 4320000 s, Cycle: 442 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00841278 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585128 s | Solve Time: 0.174054 s + compositionalMultiphaseFlow: Max pressure change: 311.598 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.687 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3724400616552686e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.18e-04 ) + Last LinSolve(iter,res) = ( 2, 8.41e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96327e+06, 1.02656e+07, 1.06499e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07611e+06, -901867 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.75e+09 s, dt: 4320000 s, Cycle: 443 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.91e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.91e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00849148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585878 s | Solve Time: 0.174182 s + compositionalMultiphaseFlow: Max pressure change: 314.869 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.351 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2441580710695916e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.22e-04 ) + Last LinSolve(iter,res) = ( 2, 8.49e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96343e+06, 1.02657e+07, 1.06502e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07587e+06, -901786 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.75e+09 s, dt: 4320000 s, Cycle: 444 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00836122 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583313 s | Solve Time: 0.175303 s + compositionalMultiphaseFlow: Max pressure change: 316.224 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.348 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0980554921455905e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.20e-04 ) + Last LinSolve(iter,res) = ( 2, 8.36e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96359e+06, 1.02657e+07, 1.06505e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07564e+06, -901709 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.76e+09 s, dt: 4320000 s, Cycle: 445 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.63e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00836827 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587969 s | Solve Time: 0.174475 s + compositionalMultiphaseFlow: Max pressure change: 318.710 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.314 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.935198031295272e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.21e-04 ) + Last LinSolve(iter,res) = ( 2, 8.37e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96375e+06, 1.02658e+07, 1.06508e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0754e+06, -901635 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.76e+09 s, dt: 4320000 s, Cycle: 446 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00834074 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585561 s | Solve Time: 0.173829 s + compositionalMultiphaseFlow: Max pressure change: 321.748 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.249 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7716478145922707e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.18e-04 ) + Last LinSolve(iter,res) = ( 2, 8.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96391e+06, 1.02658e+07, 1.06511e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07517e+06, -901516 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.76e+09 s, dt: 3000000 s, Cycle: 447 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.60e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0058785 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583563 s | Solve Time: 0.174089 s + compositionalMultiphaseFlow: Max pressure change: 222.119 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.922 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8729656972315e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.44e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.44e-05 ) + Last LinSolve(iter,res) = ( 2, 5.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96401e+06, 1.02658e+07, 1.06513e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07493e+06, -901319 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.77e+09 s, dt: 4320000 s, Cycle: 448 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.48e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.008243 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585127 s | Solve Time: 0.174744 s + compositionalMultiphaseFlow: Max pressure change: 325.866 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.208 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8629424847492757e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.19e-04 ) + Last LinSolve(iter,res) = ( 2, 8.24e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96417e+06, 1.02659e+07, 1.06516e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07478e+06, -901190 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.77e+09 s, dt: 4320000 s, Cycle: 449 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00832922 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587152 s | Solve Time: 0.174337 s + compositionalMultiphaseFlow: Max pressure change: 326.158 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.153 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.347883553133201e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.18e-04 ) + Last LinSolve(iter,res) = ( 2, 8.33e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96432e+06, 1.02659e+07, 1.06519e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07454e+06, -900995 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.78e+09 s, dt: 4320000 s, Cycle: 450 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.44e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00839589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587019 s | Solve Time: 0.173711 s + compositionalMultiphaseFlow: Max pressure change: 327.143 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.062 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2350330686204956e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.21e-04 ) + Last LinSolve(iter,res) = ( 2, 8.40e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96448e+06, 1.02659e+07, 1.06522e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07431e+06, -900811 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.9982e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.78e+09 s, dt: 4320000 s, Cycle: 451 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00843882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587213 s | Solve Time: 0.174026 s + compositionalMultiphaseFlow: Max pressure change: 329.465 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.942 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1862621479851185e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.30e-04 ) + Last LinSolve(iter,res) = ( 2, 8.44e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96463e+06, 1.0266e+07, 1.06526e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07407e+06, -900630 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.78e+09 s, dt: 4320000 s, Cycle: 452 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.39e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00841753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585118 s | Solve Time: 0.174188 s + compositionalMultiphaseFlow: Max pressure change: 330.174 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.839 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1158743290783377e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.30e-04 ) + Last LinSolve(iter,res) = ( 2, 8.42e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96478e+06, 1.0266e+07, 1.06529e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07384e+06, -900454 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.79e+09 s, dt: 4320000 s, Cycle: 453 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.39e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00834001 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586635 s | Solve Time: 0.174122 s + compositionalMultiphaseFlow: Max pressure change: 330.268 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.722 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.064116189082199e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.23e-04 ) + Last LinSolve(iter,res) = ( 2, 8.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96493e+06, 1.02661e+07, 1.06532e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07361e+06, -900282 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.79e+09 s, dt: 4320000 s, Cycle: 454 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0083392 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586118 s | Solve Time: 0.173992 s + compositionalMultiphaseFlow: Max pressure change: 331.927 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.611 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0044131820995403e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.25e-04 ) + Last LinSolve(iter,res) = ( 2, 8.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96508e+06, 1.02661e+07, 1.06535e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07338e+06, -900115 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.80e+09 s, dt: 1320000 s, Cycle: 455 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.87e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00249523 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589895 s | Solve Time: 0.17366 s + compositionalMultiphaseFlow: Max pressure change: 100.834 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.900949090336226e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.77e-06 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.77e-06 ) + Last LinSolve(iter,res) = ( 2, 2.50e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96513e+06, 1.02661e+07, 1.06536e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07314e+06, -899952 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.80e+09 s, dt: 2640000 s, Cycle: 456 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00500497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586977 s | Solve Time: 0.173639 s + compositionalMultiphaseFlow: Max pressure change: 204.516 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.143 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5057499028747756e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.62e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 4.62e-05 ) + Last LinSolve(iter,res) = ( 2, 5.00e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96522e+06, 1.02661e+07, 1.06538e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07308e+06, -899915 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.80e+09 s, dt: 4320000 s, Cycle: 457 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0082069 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5857 s | Solve Time: 0.174071 s + compositionalMultiphaseFlow: Max pressure change: 335.377 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.461 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3400724268606297e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.28e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96537e+06, 1.02662e+07, 1.06541e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07294e+06, -899811 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.81e+09 s, dt: 4320000 s, Cycle: 458 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00826694 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584376 s | Solve Time: 0.174076 s + compositionalMultiphaseFlow: Max pressure change: 337.321 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.458 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7888879266791946e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.28e-04 ) + Last LinSolve(iter,res) = ( 2, 8.27e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96552e+06, 1.02662e+07, 1.06545e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0727e+06, -899652 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.81e+09 s, dt: 4320000 s, Cycle: 459 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00828687 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588641 s | Solve Time: 0.175882 s + compositionalMultiphaseFlow: Max pressure change: 339.913 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.425 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7305940192002822e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.30e-04 ) + Last LinSolve(iter,res) = ( 2, 8.29e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96567e+06, 1.02663e+07, 1.06548e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0725e+06, -899504 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.81e+09 s, dt: 4320000 s, Cycle: 460 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00827387 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58703 s | Solve Time: 0.17444 s + compositionalMultiphaseFlow: Max pressure change: 342.521 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.406 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6560205362559088e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.31e-04 ) + Last LinSolve(iter,res) = ( 2, 8.27e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96582e+06, 1.02663e+07, 1.06551e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07233e+06, -899360 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.82e+09 s, dt: 4320000 s, Cycle: 461 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00825736 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585387 s | Solve Time: 0.174048 s + compositionalMultiphaseFlow: Max pressure change: 345.111 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.363 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5774808004298535e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.32e-04 ) + Last LinSolve(iter,res) = ( 2, 8.26e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96597e+06, 1.02663e+07, 1.06555e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07216e+06, -899221 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.82e+09 s, dt: 4320000 s, Cycle: 462 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00824071 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585868 s | Solve Time: 0.174787 s + compositionalMultiphaseFlow: Max pressure change: 347.693 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.343 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5005516484922765e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.33e-04 ) + Last LinSolve(iter,res) = ( 2, 8.24e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96611e+06, 1.02664e+07, 1.06558e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07199e+06, -899087 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.83e+09 s, dt: 3000000 s, Cycle: 463 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.51e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00574956 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585458 s | Solve Time: 0.174154 s + compositionalMultiphaseFlow: Max pressure change: 241.613 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.327 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.73527610639146e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.31e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.31e-05 ) + Last LinSolve(iter,res) = ( 2, 5.75e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96622e+06, 1.02664e+07, 1.06561e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07182e+06, -898957 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.83e+09 s, dt: 4320000 s, Cycle: 464 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.39e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0081775 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586466 s | Solve Time: 0.174217 s + compositionalMultiphaseFlow: Max pressure change: 352.978 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.347 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.724693266342726e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 8.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96636e+06, 1.02664e+07, 1.06564e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0717e+06, -898874 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.83e+09 s, dt: 4320000 s, Cycle: 465 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00818417 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584125 s | Solve Time: 0.174307 s + compositionalMultiphaseFlow: Max pressure change: 354.743 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.499 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.520843537772265e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.35e-04 ) + Last LinSolve(iter,res) = ( 2, 8.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96651e+06, 1.02665e+07, 1.06568e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07152e+06, -898747 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.84e+09 s, dt: 4320000 s, Cycle: 466 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.008182 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588372 s | Solve Time: 0.173756 s + compositionalMultiphaseFlow: Max pressure change: 357.035 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.615 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5125331287446642e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 8.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96666e+06, 1.02665e+07, 1.06571e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07134e+06, -898631 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.84e+09 s, dt: 4320000 s, Cycle: 467 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00817852 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586059 s | Solve Time: 0.173903 s + compositionalMultiphaseFlow: Max pressure change: 359.984 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.688 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5216113147253907e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.41e-04 ) + Last LinSolve(iter,res) = ( 2, 8.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9668e+06, 1.02665e+07, 1.06575e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07116e+06, -898519 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.85e+09 s, dt: 4320000 s, Cycle: 468 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00813607 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587969 s | Solve Time: 0.17402 s + compositionalMultiphaseFlow: Max pressure change: 362.069 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.734 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4864222031008012e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.42e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96695e+06, 1.02666e+07, 1.06578e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07099e+06, -898412 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.85e+09 s, dt: 4320000 s, Cycle: 469 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00813246 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584589 s | Solve Time: 0.175307 s + compositionalMultiphaseFlow: Max pressure change: 364.373 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.749 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4998056585557862e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.42e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9671e+06, 1.02666e+07, 1.06582e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07081e+06, -898309 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.86e+09 s, dt: 4320000 s, Cycle: 470 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00811145 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587249 s | Solve Time: 0.173779 s + compositionalMultiphaseFlow: Max pressure change: 366.691 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.730 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5105417805472143e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.42e-04 ) + Last LinSolve(iter,res) = ( 2, 8.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96724e+06, 1.02667e+07, 1.06585e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07063e+06, -898085 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.86e+09 s, dt: 1320000 s, Cycle: 471 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.87e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00243676 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585568 s | Solve Time: 0.173992 s + compositionalMultiphaseFlow: Max pressure change: 107.778 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.127 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.854166435586116e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.10e-05 ) + Last LinSolve(iter,res) = ( 2, 2.44e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96729e+06, 1.02667e+07, 1.06586e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07044e+06, -897856 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.86e+09 s, dt: 2640000 s, Cycle: 472 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.72e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00490339 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584062 s | Solve Time: 0.173412 s + compositionalMultiphaseFlow: Max pressure change: 225.863 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.240 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.501143367721447e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.23e-05 ) + Last LinSolve(iter,res) = ( 2, 4.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96737e+06, 1.02667e+07, 1.06589e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0704e+06, -897798 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.86e+09 s, dt: 4320000 s, Cycle: 473 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.36e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0081081 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584086 s | Solve Time: 0.173354 s + compositionalMultiphaseFlow: Max pressure change: 374.175 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.612 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3523742496432973e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 8.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96752e+06, 1.02667e+07, 1.06592e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.07028e+06, -897654 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.87e+09 s, dt: 4320000 s, Cycle: 474 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00808892 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584613 s | Solve Time: 0.173609 s + compositionalMultiphaseFlow: Max pressure change: 373.718 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.558 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5096302186101695e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.41e-04 ) + Last LinSolve(iter,res) = ( 2, 8.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96766e+06, 1.02668e+07, 1.06596e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0701e+06, -897428 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.87e+09 s, dt: 4320000 s, Cycle: 475 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00815977 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584769 s | Solve Time: 0.174039 s + compositionalMultiphaseFlow: Max pressure change: 375.545 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.510 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5190198188186343e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.44e-04 ) + Last LinSolve(iter,res) = ( 2, 8.16e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96781e+06, 1.02668e+07, 1.066e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06991e+06, -897212 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.88e+09 s, dt: 4320000 s, Cycle: 476 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00814409 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585717 s | Solve Time: 0.174051 s + compositionalMultiphaseFlow: Max pressure change: 378.026 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.428 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5053535940001694e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96795e+06, 1.02668e+07, 1.06604e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06973e+06, -896999 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.88e+09 s, dt: 4320000 s, Cycle: 477 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0080478 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.591576 s | Solve Time: 0.173812 s + compositionalMultiphaseFlow: Max pressure change: 379.723 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.321 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4894888855643273e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 8.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9681e+06, 1.02669e+07, 1.06607e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06954e+06, -896790 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.89e+09 s, dt: 4320000 s, Cycle: 478 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00805779 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586375 s | Solve Time: 0.173525 s + compositionalMultiphaseFlow: Max pressure change: 381.912 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.279 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4962679872887463e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96824e+06, 1.02669e+07, 1.06611e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06936e+06, -896585 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.89e+09 s, dt: 3000000 s, Cycle: 479 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.53e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00556013 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586577 s | Solve Time: 0.173661 s + compositionalMultiphaseFlow: Max pressure change: 262.395 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.267 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7399740757383384e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.96e-05 ) + Last LinSolve(iter,res) = ( 2, 5.56e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96834e+06, 1.02669e+07, 1.06614e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06917e+06, -896384 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.89e+09 s, dt: 4320000 s, Cycle: 480 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00798038 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584705 s | Solve Time: 0.173679 s + compositionalMultiphaseFlow: Max pressure change: 387.434 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.223 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7024134928721466e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96849e+06, 1.0267e+07, 1.06618e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06904e+06, -896252 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.90e+09 s, dt: 4320000 s, Cycle: 481 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0079869 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586498 s | Solve Time: 0.17375 s + compositionalMultiphaseFlow: Max pressure change: 386.316 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.221 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5244512352463602e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96863e+06, 1.0267e+07, 1.06621e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06885e+06, -896054 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.90e+09 s, dt: 4320000 s, Cycle: 482 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00798784 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584284 s | Solve Time: 0.173589 s + compositionalMultiphaseFlow: Max pressure change: 387.922 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.289 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.515631666837436e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96877e+06, 1.0267e+07, 1.06625e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06867e+06, -895865 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.91e+09 s, dt: 4320000 s, Cycle: 483 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00797811 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586555 s | Solve Time: 0.173727 s + compositionalMultiphaseFlow: Max pressure change: 389.496 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.323 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5347923765229865e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 7.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96891e+06, 1.02671e+07, 1.06629e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06848e+06, -895680 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.91e+09 s, dt: 4320000 s, Cycle: 484 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.39e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00792349 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.589628 s | Solve Time: 0.173989 s + compositionalMultiphaseFlow: Max pressure change: 391.361 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.325 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5375384132543246e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.92e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96906e+06, 1.02671e+07, 1.06633e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06829e+06, -895500 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.92e+09 s, dt: 4320000 s, Cycle: 485 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00794825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587508 s | Solve Time: 0.173382 s + compositionalMultiphaseFlow: Max pressure change: 392.799 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.300 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5531118968681312e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9692e+06, 1.02671e+07, 1.06637e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0681e+06, -895323 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.92e+09 s, dt: 4320000 s, Cycle: 486 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00790505 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.584122 s | Solve Time: 0.174488 s + compositionalMultiphaseFlow: Max pressure change: 393.742 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.239 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.523257471269801e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96934e+06, 1.02672e+07, 1.06641e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06791e+06, -895151 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.92e+09 s, dt: 1320000 s, Cycle: 487 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.88e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.88e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00241548 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585116 s | Solve Time: 0.173912 s + compositionalMultiphaseFlow: Max pressure change: 111.951 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.996 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.730543790465447e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.19e-05 ) + Last LinSolve(iter,res) = ( 2, 2.42e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96939e+06, 1.02672e+07, 1.06642e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06773e+06, -894983 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.93e+09 s, dt: 2640000 s, Cycle: 488 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.75e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00482634 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586303 s | Solve Time: 0.173935 s + compositionalMultiphaseFlow: Max pressure change: 243.942 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 23.951 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4628280227135804e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.53e-05 ) + Last LinSolve(iter,res) = ( 2, 4.83e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96947e+06, 1.02672e+07, 1.06645e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06767e+06, -894943 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.93e+09 s, dt: 4320000 s, Cycle: 489 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0078456 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586189 s | Solve Time: 0.173582 s + compositionalMultiphaseFlow: Max pressure change: 400.957 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.177 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.249951331274481e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.85e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96962e+06, 1.02672e+07, 1.06649e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06756e+06, -894837 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.93e+09 s, dt: 4320000 s, Cycle: 490 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00790504 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585399 s | Solve Time: 0.173979 s + compositionalMultiphaseFlow: Max pressure change: 396.821 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.220 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5699371336275192e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.96976e+06, 1.02673e+07, 1.06652e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06736e+06, -894657 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.94e+09 s, dt: 4320000 s, Cycle: 491 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00791015 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585204 s | Solve Time: 0.173974 s + compositionalMultiphaseFlow: Max pressure change: 397.790 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.233 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.58742809230894e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9699e+06, 1.02673e+07, 1.06656e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06717e+06, -894358 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.94e+09 s, dt: 4320000 s, Cycle: 492 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00791038 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590307 s | Solve Time: 0.173712 s + compositionalMultiphaseFlow: Max pressure change: 398.500 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.214 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5787228979657897e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97004e+06, 1.02673e+07, 1.0666e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06698e+06, -894061 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.95e+09 s, dt: 4320000 s, Cycle: 493 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0079099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585319 s | Solve Time: 0.17412 s + compositionalMultiphaseFlow: Max pressure change: 399.092 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.164 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5633994865371648e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97018e+06, 1.02674e+07, 1.06664e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06679e+06, -893766 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.95e+09 s, dt: 4320000 s, Cycle: 494 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0079091 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.591194 s | Solve Time: 0.173947 s + compositionalMultiphaseFlow: Max pressure change: 399.581 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.136 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5755627946756334e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97032e+06, 1.02674e+07, 1.06668e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0666e+06, -893475 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.95e+09 s, dt: 3000000 s, Cycle: 495 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.54e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00551838 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585181 s | Solve Time: 0.174105 s + compositionalMultiphaseFlow: Max pressure change: 272.425 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.173 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6821505483276553e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.78e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.78e-05 ) + Last LinSolve(iter,res) = ( 2, 5.52e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97042e+06, 1.02674e+07, 1.06671e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06641e+06, -893186 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.96e+09 s, dt: 4320000 s, Cycle: 496 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00782598 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.588008 s | Solve Time: 0.173967 s + compositionalMultiphaseFlow: Max pressure change: 405.407 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.106 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6737884190053407e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.83e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97056e+06, 1.02674e+07, 1.06675e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06628e+06, -892993 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.96e+09 s, dt: 4320000 s, Cycle: 497 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.007861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583718 s | Solve Time: 0.17397 s + compositionalMultiphaseFlow: Max pressure change: 400.387 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.155 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6018192161570965e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.44e-04 ) + Last LinSolve(iter,res) = ( 2, 7.86e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9707e+06, 1.02675e+07, 1.06679e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06609e+06, -892704 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.97e+09 s, dt: 4320000 s, Cycle: 498 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00791302 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.58808 s | Solve Time: 0.174205 s + compositionalMultiphaseFlow: Max pressure change: 400.403 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.172 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6208468922584984e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97084e+06, 1.02675e+07, 1.06683e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0659e+06, -892424 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 1.97e+09 s, dt: 4320000 s, Cycle: 499 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00806467 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.587013 s | Solve Time: 0.17424 s + compositionalMultiphaseFlow: Max pressure change: 400.549 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.158 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6122678192509454e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.42e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97098e+06, 1.02675e+07, 1.06687e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06571e+06, -892146 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.97e+09 s, dt: 4320000 s, Cycle: 500 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0080756 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.585271 s | Solve Time: 0.174194 s + compositionalMultiphaseFlow: Max pressure change: 400.353 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.148 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.612259510341829e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 8.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97112e+06, 1.02676e+07, 1.06691e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06552e+06, -891872 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.98e+09 s, dt: 4320000 s, Cycle: 501 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00808927 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583742 s | Solve Time: 0.174185 s + compositionalMultiphaseFlow: Max pressure change: 399.974 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.201 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5849239554110994e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.44e-04 ) + Last LinSolve(iter,res) = ( 2, 8.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97126e+06, 1.02676e+07, 1.06695e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06533e+06, -891601 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.98e+09 s, dt: 4320000 s, Cycle: 502 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.37e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.37e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00807738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586906 s | Solve Time: 0.17371 s + compositionalMultiphaseFlow: Max pressure change: 399.715 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.256 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.620184987283224e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.45e-04 ) + Last LinSolve(iter,res) = ( 2, 8.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9714e+06, 1.02676e+07, 1.06699e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06514e+06, -891333 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.99e+09 s, dt: 1320000 s, Cycle: 503 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.87e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00241881 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.582857 s | Solve Time: 0.174091 s + compositionalMultiphaseFlow: Max pressure change: 110.022 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.998 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.682466819838638e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.30e-05 ) + Last LinSolve(iter,res) = ( 2, 2.42e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97145e+06, 1.02676e+07, 1.067e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06495e+06, -891069 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.99e+09 s, dt: 2640000 s, Cycle: 504 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.75e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00475616 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586805 s | Solve Time: 0.173528 s + compositionalMultiphaseFlow: Max pressure change: 249.043 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.000 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4561639023469297e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.45e-05 ) + Last LinSolve(iter,res) = ( 2, 4.76e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97153e+06, 1.02677e+07, 1.06703e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0649e+06, -890991 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 1.99e+09 s, dt: 4320000 s, Cycle: 505 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00779138 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583045 s | Solve Time: 0.173871 s + compositionalMultiphaseFlow: Max pressure change: 404.963 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.274 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2626348923647797e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.79e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97167e+06, 1.02677e+07, 1.06707e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06478e+06, -890744 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 2.00e+09 s, dt: 4320000 s, Cycle: 506 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.45e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00789879 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.590155 s | Solve Time: 0.174526 s + compositionalMultiphaseFlow: Max pressure change: 397.347 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.347 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.660368396105838e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97181e+06, 1.02677e+07, 1.06711e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06459e+06, -890341 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 2.00e+09 s, dt: 4320000 s, Cycle: 507 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.46e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00793596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.583995 s | Solve Time: 0.174572 s + compositionalMultiphaseFlow: Max pressure change: 396.659 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.451 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6435403260572912e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97195e+06, 1.02678e+07, 1.06714e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0644e+06, -889946 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 2.00e+09 s, dt: 4320000 s, Cycle: 508 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.46e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00796811 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.586207 s | Solve Time: 0.174107 s + compositionalMultiphaseFlow: Max pressure change: 395.680 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.522 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.660868483854827e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.97e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97209e+06, 1.02678e+07, 1.06718e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06421e+06, -889552 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69929e+11 } } mol +Time: 2.01e+09 s, dt: 4320000 s, Cycle: 509 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.45e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00790618 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602352 s | Solve Time: 0.173596 s + compositionalMultiphaseFlow: Max pressure change: 394.667 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.558 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.622831508063527e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97223e+06, 1.02678e+07, 1.06722e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06402e+06, -889159 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.01e+09 s, dt: 4320000 s, Cycle: 510 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.48e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00791667 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602732 s | Solve Time: 0.174141 s + compositionalMultiphaseFlow: Max pressure change: 393.158 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.561 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6153154613895992e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.92e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97237e+06, 1.02678e+07, 1.06726e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06383e+06, -888767 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.02e+09 s, dt: 3000000 s, Cycle: 511 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.59e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00557735 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.6068 s | Solve Time: 0.173804 s + compositionalMultiphaseFlow: Max pressure change: 265.951 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.473 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.720592725991011e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.35e-05 ) + Last LinSolve(iter,res) = ( 2, 5.58e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97246e+06, 1.02679e+07, 1.06729e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06364e+06, -888377 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.02e+09 s, dt: 4320000 s, Cycle: 512 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.50e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.50e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00787733 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601686 s | Solve Time: 0.174334 s + compositionalMultiphaseFlow: Max pressure change: 396.731 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.498 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.731398777378047e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.52e-04 ) + Last LinSolve(iter,res) = ( 2, 7.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9726e+06, 1.02679e+07, 1.06733e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06351e+06, -888113 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.02e+09 s, dt: 4320000 s, Cycle: 513 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599061 s | Solve Time: 0.173918 s + compositionalMultiphaseFlow: Max pressure change: 389.306 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.611 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6704464667061103e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.53e-04 ) + Last LinSolve(iter,res) = ( 2, 7.97e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97274e+06, 1.02679e+07, 1.06737e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06332e+06, -887719 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.03e+09 s, dt: 4320000 s, Cycle: 514 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00794242 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598452 s | Solve Time: 0.174818 s + compositionalMultiphaseFlow: Max pressure change: 387.206 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.690 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6779781697451313e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.55e-04 ) + Last LinSolve(iter,res) = ( 2, 7.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97288e+06, 1.0268e+07, 1.06741e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06313e+06, -887333 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.03e+09 s, dt: 4320000 s, Cycle: 515 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.51e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00799047 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.631423 s | Solve Time: 0.173861 s + compositionalMultiphaseFlow: Max pressure change: 384.931 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.731 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.697833691416406e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.57e-04 ) + Last LinSolve(iter,res) = ( 2, 7.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97301e+06, 1.0268e+07, 1.06744e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06294e+06, -886949 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.04e+09 s, dt: 4320000 s, Cycle: 516 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00805124 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602814 s | Solve Time: 0.174263 s + compositionalMultiphaseFlow: Max pressure change: 383.416 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.744 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6759086152173808e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 8.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97315e+06, 1.0268e+07, 1.06748e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06275e+06, -886567 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.04e+09 s, dt: 4320000 s, Cycle: 517 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00806468 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606792 s | Solve Time: 0.173319 s + compositionalMultiphaseFlow: Max pressure change: 381.687 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.724 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.659932831188371e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.60e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97329e+06, 1.0268e+07, 1.06752e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06257e+06, -886187 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.05e+09 s, dt: 4320000 s, Cycle: 518 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00807776 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601348 s | Solve Time: 0.174747 s + compositionalMultiphaseFlow: Max pressure change: 379.720 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.681 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6497174826213268e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-04 ) + Last LinSolve(iter,res) = ( 2, 8.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97342e+06, 1.02681e+07, 1.06756e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06238e+06, -885809 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.05e+09 s, dt: 1320000 s, Cycle: 519 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0024678 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59989 s | Solve Time: 0.174564 s + compositionalMultiphaseFlow: Max pressure change: 102.058 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.154 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.818216568169831e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-05 ) + Last LinSolve(iter,res) = ( 2, 2.47e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97347e+06, 1.02681e+07, 1.06757e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06219e+06, -885433 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.05e+09 s, dt: 2640000 s, Cycle: 520 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.85e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00493691 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602463 s | Solve Time: 0.174728 s + compositionalMultiphaseFlow: Max pressure change: 238.113 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.341 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4931687792874015e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.25e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.25e-05 ) + Last LinSolve(iter,res) = ( 2, 4.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97355e+06, 1.02681e+07, 1.06759e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06214e+06, -885332 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.05e+09 s, dt: 4320000 s, Cycle: 521 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.59e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00798673 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602981 s | Solve Time: 0.173648 s + compositionalMultiphaseFlow: Max pressure change: 382.897 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.912 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3381029279633267e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-04 ) + Last LinSolve(iter,res) = ( 2, 7.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97369e+06, 1.02681e+07, 1.06763e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06204e+06, -885097 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.06e+09 s, dt: 4320000 s, Cycle: 522 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.60e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00809053 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603246 s | Solve Time: 0.173885 s + compositionalMultiphaseFlow: Max pressure change: 372.776 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.980 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6833664917559332e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.63e-04 ) + Last LinSolve(iter,res) = ( 2, 8.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97382e+06, 1.02682e+07, 1.06767e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06188e+06, -884718 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.06e+09 s, dt: 4320000 s, Cycle: 523 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.58e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.58e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00812811 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601681 s | Solve Time: 0.173112 s + compositionalMultiphaseFlow: Max pressure change: 370.860 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.012 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7270664176560757e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.64e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97396e+06, 1.02682e+07, 1.0677e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06172e+06, -884349 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.07e+09 s, dt: 4320000 s, Cycle: 524 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00812762 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600211 s | Solve Time: 0.17417 s + compositionalMultiphaseFlow: Max pressure change: 368.000 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.009 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7175724342788357e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.64e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9741e+06, 1.02682e+07, 1.06774e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06156e+06, -883983 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.07e+09 s, dt: 4320000 s, Cycle: 525 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.60e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00814145 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606121 s | Solve Time: 0.171489 s + compositionalMultiphaseFlow: Max pressure change: 365.403 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.974 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7145441066901412e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.64e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97423e+06, 1.02682e+07, 1.06777e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0614e+06, -883620 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.08e+09 s, dt: 4320000 s, Cycle: 526 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.62e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.62e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00810456 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600709 s | Solve Time: 0.173433 s + compositionalMultiphaseFlow: Max pressure change: 363.029 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.963 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7308121935677434e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.63e-04 ) + Last LinSolve(iter,res) = ( 2, 8.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97437e+06, 1.02683e+07, 1.06781e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06124e+06, -883260 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.08e+09 s, dt: 3000000 s, Cycle: 527 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.69e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00563702 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606265 s | Solve Time: 0.174813 s + compositionalMultiphaseFlow: Max pressure change: 244.464 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.807 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7852921097304417e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.07e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.07e-05 ) + Last LinSolve(iter,res) = ( 2, 5.64e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97446e+06, 1.02683e+07, 1.06783e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06108e+06, -882903 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.08e+09 s, dt: 4320000 s, Cycle: 528 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.64e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0080587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.611589 s | Solve Time: 0.174541 s + compositionalMultiphaseFlow: Max pressure change: 365.714 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.151 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.797616630689781e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.66e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9746e+06, 1.02683e+07, 1.06787e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06097e+06, -882663 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.09e+09 s, dt: 4320000 s, Cycle: 529 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.64e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00811108 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601606 s | Solve Time: 0.173907 s + compositionalMultiphaseFlow: Max pressure change: 355.629 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.234 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.804222895529506e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.66e-04 ) + Last LinSolve(iter,res) = ( 2, 8.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97473e+06, 1.02683e+07, 1.0679e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0608e+06, -882303 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69928e+11 } } mol +Time: 2.09e+09 s, dt: 4320000 s, Cycle: 530 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.64e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00814457 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602134 s | Solve Time: 0.174956 s + compositionalMultiphaseFlow: Max pressure change: 353.252 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.277 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8227669928982948e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.68e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97487e+06, 1.02684e+07, 1.06794e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06064e+06, -881955 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.10e+09 s, dt: 4320000 s, Cycle: 531 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.64e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00815439 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600898 s | Solve Time: 0.174274 s + compositionalMultiphaseFlow: Max pressure change: 350.545 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.285 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8213419938906128e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.69e-04 ) + Last LinSolve(iter,res) = ( 2, 8.15e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.975e+06, 1.02684e+07, 1.06797e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06048e+06, -881609 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.10e+09 s, dt: 4320000 s, Cycle: 532 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.63e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.63e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00812553 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603604 s | Solve Time: 0.174323 s + compositionalMultiphaseFlow: Max pressure change: 347.559 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.258 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.814559379420544e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.71e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97514e+06, 1.02684e+07, 1.06801e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06032e+06, -881266 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.10e+09 s, dt: 4320000 s, Cycle: 533 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00814408 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600526 s | Solve Time: 0.173444 s + compositionalMultiphaseFlow: Max pressure change: 344.813 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.212 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.829960253330043e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.72e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97527e+06, 1.02685e+07, 1.06804e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.06016e+06, -880927 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.11e+09 s, dt: 4320000 s, Cycle: 534 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.68e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.68e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00815196 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600039 s | Solve Time: 0.174495 s + compositionalMultiphaseFlow: Max pressure change: 342.148 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.191 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.86532675749973e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.73e-04 ) + Last LinSolve(iter,res) = ( 2, 8.15e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97541e+06, 1.02685e+07, 1.06807e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05999e+06, -880592 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.11e+09 s, dt: 1320000 s, Cycle: 535 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.96e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.96e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00249058 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605335 s | Solve Time: 0.174114 s + compositionalMultiphaseFlow: Max pressure change: 90.971 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.297 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.931994204371293e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-05 ) + Last LinSolve(iter,res) = ( 2, 2.49e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97545e+06, 1.02685e+07, 1.06808e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05983e+06, -880260 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.11e+09 s, dt: 2640000 s, Cycle: 536 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.92e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00488844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606238 s | Solve Time: 0.174068 s + compositionalMultiphaseFlow: Max pressure change: 215.304 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.574 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5271501557778677e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.70e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.70e-05 ) + Last LinSolve(iter,res) = ( 2, 4.89e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97553e+06, 1.02685e+07, 1.0681e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05978e+06, -880175 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.12e+09 s, dt: 4320000 s, Cycle: 537 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.71e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00804034 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605903 s | Solve Time: 0.173903 s + compositionalMultiphaseFlow: Max pressure change: 344.187 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.302 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3968072730150567e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 8.04e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97566e+06, 1.02685e+07, 1.06814e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05968e+06, -879966 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.12e+09 s, dt: 4320000 s, Cycle: 538 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.71e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00815017 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602627 s | Solve Time: 0.174061 s + compositionalMultiphaseFlow: Max pressure change: 333.631 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.381 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9323178301888788e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.75e-04 ) + Last LinSolve(iter,res) = ( 2, 8.15e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9758e+06, 1.02686e+07, 1.06817e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05952e+06, -879632 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.13e+09 s, dt: 4320000 s, Cycle: 539 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.70e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00818642 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602325 s | Solve Time: 0.17363 s + compositionalMultiphaseFlow: Max pressure change: 331.534 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.421 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9250425620231937e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.77e-04 ) + Last LinSolve(iter,res) = ( 2, 8.19e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97593e+06, 1.02686e+07, 1.0682e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05936e+06, -879312 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.13e+09 s, dt: 4320000 s, Cycle: 540 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.69e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00820322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598935 s | Solve Time: 0.173781 s + compositionalMultiphaseFlow: Max pressure change: 328.835 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.426 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.931201628613266e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.77e-04 ) + Last LinSolve(iter,res) = ( 2, 8.20e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97606e+06, 1.02686e+07, 1.06823e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05919e+06, -878994 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.13e+09 s, dt: 4320000 s, Cycle: 541 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.69e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00821695 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601288 s | Solve Time: 0.174204 s + compositionalMultiphaseFlow: Max pressure change: 326.168 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.397 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.905197098972522e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.78e-04 ) + Last LinSolve(iter,res) = ( 2, 8.22e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9762e+06, 1.02686e+07, 1.06826e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05903e+06, -878681 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.14e+09 s, dt: 4320000 s, Cycle: 542 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.69e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00821441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605677 s | Solve Time: 0.174043 s + compositionalMultiphaseFlow: Max pressure change: 323.427 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.335 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9198104195261578e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.78e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97633e+06, 1.02687e+07, 1.06829e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05887e+06, -878371 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.14e+09 s, dt: 3000000 s, Cycle: 543 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.74e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00564315 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601986 s | Solve Time: 0.174429 s + compositionalMultiphaseFlow: Max pressure change: 217.471 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 28.012 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8362519921554252e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.66e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.66e-05 ) + Last LinSolve(iter,res) = ( 2, 5.64e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97642e+06, 1.02687e+07, 1.06831e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0587e+06, -878065 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.15e+09 s, dt: 4320000 s, Cycle: 544 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.70e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.70e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00814482 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603836 s | Solve Time: 0.172353 s + compositionalMultiphaseFlow: Max pressure change: 325.424 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.373 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8295598003547084e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.78e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97656e+06, 1.02687e+07, 1.06834e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05859e+06, -877862 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.15e+09 s, dt: 4320000 s, Cycle: 545 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.71e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00819138 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60345 s | Solve Time: 0.174045 s + compositionalMultiphaseFlow: Max pressure change: 316.098 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.426 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0139929224338715e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.78e-04 ) + Last LinSolve(iter,res) = ( 2, 8.19e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97669e+06, 1.02687e+07, 1.06837e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05842e+06, -877556 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99819e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.15e+09 s, dt: 4320000 s, Cycle: 546 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.77e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00820994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601468 s | Solve Time: 0.174605 s + compositionalMultiphaseFlow: Max pressure change: 313.408 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.467 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0219687157929656e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97682e+06, 1.02688e+07, 1.0684e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05826e+06, -877262 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.16e+09 s, dt: 4320000 s, Cycle: 547 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.82e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.82e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00820756 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606468 s | Solve Time: 0.173899 s + compositionalMultiphaseFlow: Max pressure change: 310.776 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.608 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0330991046257907e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.78e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97695e+06, 1.02688e+07, 1.06843e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0581e+06, -876971 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.16e+09 s, dt: 4320000 s, Cycle: 548 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.85e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.85e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00820862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.610418 s | Solve Time: 0.173952 s + compositionalMultiphaseFlow: Max pressure change: 308.177 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.803 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.999905211436115e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.77e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97708e+06, 1.02688e+07, 1.06846e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05793e+06, -876685 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69927e+11 } } mol +Time: 2.17e+09 s, dt: 4320000 s, Cycle: 549 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.87e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.87e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0082096 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605951 s | Solve Time: 0.17419 s + compositionalMultiphaseFlow: Max pressure change: 305.515 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.953 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9983202803608435e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.77e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97722e+06, 1.02688e+07, 1.06849e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05777e+06, -876403 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.17e+09 s, dt: 4320000 s, Cycle: 550 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.88e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00822044 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603233 s | Solve Time: 0.174254 s + compositionalMultiphaseFlow: Max pressure change: 302.830 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.076 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9933632300350723e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.77e-04 ) + Last LinSolve(iter,res) = ( 2, 8.22e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97735e+06, 1.02689e+07, 1.06852e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05761e+06, -876125 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.18e+09 s, dt: 1320000 s, Cycle: 551 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.02e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.02e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00250992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602103 s | Solve Time: 0.173837 s + compositionalMultiphaseFlow: Max pressure change: 90.939 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.578 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.060597105921438e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.63e-05 ) + Last LinSolve(iter,res) = ( 2, 2.51e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97739e+06, 1.02689e+07, 1.06852e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05744e+06, -875852 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.18e+09 s, dt: 2640000 s, Cycle: 552 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.04e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00510314 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599055 s | Solve Time: 0.173643 s + compositionalMultiphaseFlow: Max pressure change: 190.983 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25.173 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5819105502190567e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.94e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.94e-05 ) + Last LinSolve(iter,res) = ( 2, 5.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97747e+06, 1.02689e+07, 1.06854e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0574e+06, -875785 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.18e+09 s, dt: 4320000 s, Cycle: 553 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.92e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00808565 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59827 s | Solve Time: 0.173734 s + compositionalMultiphaseFlow: Max pressure change: 304.628 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.260 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.5605220222167944e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.78e-04 ) + Last LinSolve(iter,res) = ( 2, 8.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9776e+06, 1.02689e+07, 1.06857e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0573e+06, -875612 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.18e+09 s, dt: 4320000 s, Cycle: 554 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.97e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.97e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00818379 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.5994 s | Solve Time: 0.173763 s + compositionalMultiphaseFlow: Max pressure change: 294.495 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.299 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0471290707035905e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 2, 8.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97773e+06, 1.02689e+07, 1.06859e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05713e+06, -875338 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.19e+09 s, dt: 4320000 s, Cycle: 555 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00804789 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601822 s | Solve Time: 0.17381 s + compositionalMultiphaseFlow: Max pressure change: 292.290 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.358 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0871892314477947e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 8.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97786e+06, 1.0269e+07, 1.06862e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05697e+06, -875078 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.19e+09 s, dt: 4320000 s, Cycle: 556 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00806229 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602659 s | Solve Time: 0.174145 s + compositionalMultiphaseFlow: Max pressure change: 290.280 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.556 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0905244668689704e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97799e+06, 1.0269e+07, 1.06864e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05681e+06, -874821 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.20e+09 s, dt: 4320000 s, Cycle: 557 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0080641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601099 s | Solve Time: 0.174762 s + compositionalMultiphaseFlow: Max pressure change: 287.834 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.706 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0852478754829207e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97812e+06, 1.0269e+07, 1.06867e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05664e+06, -874569 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.20e+09 s, dt: 4320000 s, Cycle: 558 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00806535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600553 s | Solve Time: 0.174039 s + compositionalMultiphaseFlow: Max pressure change: 285.612 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.848 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1774551683950705e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.07e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97825e+06, 1.0269e+07, 1.06869e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05648e+06, -874321 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.21e+09 s, dt: 3000000 s, Cycle: 559 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.01e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.01e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00567542 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606703 s | Solve Time: 0.173887 s + compositionalMultiphaseFlow: Max pressure change: 200.266 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29.137 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.97921176295457e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.96e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.96e-05 ) + Last LinSolve(iter,res) = ( 2, 5.68e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97834e+06, 1.02691e+07, 1.06871e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05632e+06, -874078 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66546e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.21e+09 s, dt: 4320000 s, Cycle: 560 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00797773 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601934 s | Solve Time: 0.174416 s + compositionalMultiphaseFlow: Max pressure change: 287.471 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.013 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.055302164933771e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 7.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97847e+06, 1.02691e+07, 1.06873e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05621e+06, -873919 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69926e+11 } } mol +Time: 2.21e+09 s, dt: 4320000 s, Cycle: 561 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00799087 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605347 s | Solve Time: 0.17467 s + compositionalMultiphaseFlow: Max pressure change: 284.699 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.055 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1100054736766793e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 7.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97859e+06, 1.02691e+07, 1.06876e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05604e+06, -873675 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.22e+09 s, dt: 4320000 s, Cycle: 562 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00801567 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600144 s | Solve Time: 0.173968 s + compositionalMultiphaseFlow: Max pressure change: 285.235 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.051 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2003248900670513e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 8.02e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97872e+06, 1.02691e+07, 1.06878e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05588e+06, -873444 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.22e+09 s, dt: 4320000 s, Cycle: 563 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00801807 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599577 s | Solve Time: 0.174034 s + compositionalMultiphaseFlow: Max pressure change: 285.544 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.022 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2391706833158054e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.85e-04 ) + Last LinSolve(iter,res) = ( 2, 8.02e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97885e+06, 1.02691e+07, 1.0688e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05572e+06, -873217 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.23e+09 s, dt: 4320000 s, Cycle: 564 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00810961 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598656 s | Solve Time: 0.175 s + compositionalMultiphaseFlow: Max pressure change: 285.889 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.212 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1066776123568332e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97898e+06, 1.02692e+07, 1.06882e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05556e+06, -872995 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.23e+09 s, dt: 4320000 s, Cycle: 565 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00810892 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601818 s | Solve Time: 0.173505 s + compositionalMultiphaseFlow: Max pressure change: 285.910 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.353 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3021103001674703e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97911e+06, 1.02692e+07, 1.06884e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0554e+06, -872776 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.24e+09 s, dt: 4320000 s, Cycle: 566 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0081053 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599499 s | Solve Time: 0.174167 s + compositionalMultiphaseFlow: Max pressure change: 286.001 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.450 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2412713240882454e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97924e+06, 1.02692e+07, 1.06886e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05524e+06, -872563 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.24e+09 s, dt: 1320000 s, Cycle: 567 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.13e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.13e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00250263 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600258 s | Solve Time: 0.17419 s + compositionalMultiphaseFlow: Max pressure change: 91.659 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13.001 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.404863109959024e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.72e-05 ) + Last LinSolve(iter,res) = ( 2, 2.50e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97928e+06, 1.02692e+07, 1.06887e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05508e+06, -872353 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.24e+09 s, dt: 2640000 s, Cycle: 568 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.24e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00487664 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.611965 s | Solve Time: 0.174339 s + compositionalMultiphaseFlow: Max pressure change: 174.318 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.007 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6884968027097713e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.07e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.07e-05 ) + Last LinSolve(iter,res) = ( 2, 4.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97935e+06, 1.02692e+07, 1.06888e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05503e+06, -872306 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.24e+09 s, dt: 4320000 s, Cycle: 569 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00792611 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602202 s | Solve Time: 0.173358 s + compositionalMultiphaseFlow: Max pressure change: 283.086 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.615 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7981294800371046e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 7.93e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97948e+06, 1.02693e+07, 1.0689e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05493e+06, -872173 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.25e+09 s, dt: 4320000 s, Cycle: 570 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0080922 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599357 s | Solve Time: 0.173928 s + compositionalMultiphaseFlow: Max pressure change: 286.362 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.631 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3146721228606282e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97961e+06, 1.02693e+07, 1.06892e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05477e+06, -871963 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.25e+09 s, dt: 4320000 s, Cycle: 571 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00813875 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599039 s | Solve Time: 0.174381 s + compositionalMultiphaseFlow: Max pressure change: 286.643 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.604 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4393700515101813e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97973e+06, 1.02693e+07, 1.06894e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05461e+06, -871767 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.26e+09 s, dt: 4320000 s, Cycle: 572 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00813944 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604678 s | Solve Time: 0.173709 s + compositionalMultiphaseFlow: Max pressure change: 286.711 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.532 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2238814090247416e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97986e+06, 1.02693e+07, 1.06896e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05445e+06, -871576 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69925e+11 } } mol +Time: 2.26e+09 s, dt: 4320000 s, Cycle: 573 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0081342 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600078 s | Solve Time: 0.173337 s + compositionalMultiphaseFlow: Max pressure change: 286.720 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.566 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2839445978917183e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.97999e+06, 1.02694e+07, 1.06898e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05429e+06, -871388 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.26e+09 s, dt: 4320000 s, Cycle: 574 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00812698 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598227 s | Solve Time: 0.173805 s + compositionalMultiphaseFlow: Max pressure change: 286.742 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.716 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2630284013391844e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98011e+06, 1.02694e+07, 1.069e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05413e+06, -871205 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.27e+09 s, dt: 3000000 s, Cycle: 575 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.18e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.18e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00564068 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602377 s | Solve Time: 0.174034 s + compositionalMultiphaseFlow: Max pressure change: 201.433 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29.733 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.133906633756567e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.73e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.73e-05 ) + Last LinSolve(iter,res) = ( 2, 5.64e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9802e+06, 1.02694e+07, 1.06901e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05397e+06, -871027 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.27e+09 s, dt: 4320000 s, Cycle: 576 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00802651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603262 s | Solve Time: 0.17488 s + compositionalMultiphaseFlow: Max pressure change: 284.656 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.918 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.1824635997601547e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 2, 8.03e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98033e+06, 1.02694e+07, 1.06903e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05386e+06, -870912 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.28e+09 s, dt: 4320000 s, Cycle: 577 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00808127 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602258 s | Solve Time: 0.173704 s + compositionalMultiphaseFlow: Max pressure change: 286.526 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.997 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3999006193431427e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 2, 8.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98045e+06, 1.02694e+07, 1.06904e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0537e+06, -870733 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.28e+09 s, dt: 4320000 s, Cycle: 578 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00809535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601971 s | Solve Time: 0.173929 s + compositionalMultiphaseFlow: Max pressure change: 286.751 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.027 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3354900346994611e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 8.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98058e+06, 1.02695e+07, 1.06906e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05354e+06, -870566 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.29e+09 s, dt: 4320000 s, Cycle: 579 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0080911 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598884 s | Solve Time: 0.174146 s + compositionalMultiphaseFlow: Max pressure change: 286.716 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.011 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5867059305628715e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9807e+06, 1.02695e+07, 1.06908e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05339e+06, -870404 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.29e+09 s, dt: 4320000 s, Cycle: 580 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00808387 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600176 s | Solve Time: 0.173804 s + compositionalMultiphaseFlow: Max pressure change: 286.678 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.951 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.7398127555589014e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98082e+06, 1.02695e+07, 1.06909e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05323e+06, -870245 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.29e+09 s, dt: 4320000 s, Cycle: 581 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00807563 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603974 s | Solve Time: 0.173957 s + compositionalMultiphaseFlow: Max pressure change: 286.611 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.849 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8230347670632483e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.82e-04 ) + Last LinSolve(iter,res) = ( 2, 8.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98095e+06, 1.02695e+07, 1.06911e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05307e+06, -870091 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26564e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69924e+11 } } mol +Time: 2.30e+09 s, dt: 4320000 s, Cycle: 582 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.008049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603563 s | Solve Time: 0.174074 s + compositionalMultiphaseFlow: Max pressure change: 286.323 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.770 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5435283013131027e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.82e-04 ) + Last LinSolve(iter,res) = ( 2, 8.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98107e+06, 1.02695e+07, 1.06912e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05291e+06, -869941 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.30e+09 s, dt: 1320000 s, Cycle: 583 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.16e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00247528 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602339 s | Solve Time: 0.175469 s + compositionalMultiphaseFlow: Max pressure change: 91.594 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.576615393798612e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.65e-05 ) + Last LinSolve(iter,res) = ( 2, 2.48e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98111e+06, 1.02695e+07, 1.06912e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05276e+06, -869795 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.30e+09 s, dt: 2640000 s, Cycle: 584 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.32e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0049855 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602222 s | Solve Time: 0.174274 s + compositionalMultiphaseFlow: Max pressure change: 174.698 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.151 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.719401371613749e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.04e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.04e-05 ) + Last LinSolve(iter,res) = ( 2, 4.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98118e+06, 1.02696e+07, 1.06913e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05271e+06, -869766 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.31e+09 s, dt: 4320000 s, Cycle: 585 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0078623 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601315 s | Solve Time: 0.173844 s + compositionalMultiphaseFlow: Max pressure change: 283.135 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.927 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.830793489201234e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 7.86e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98131e+06, 1.02696e+07, 1.06915e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05262e+06, -869672 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.31e+09 s, dt: 4320000 s, Cycle: 586 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0079825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600131 s | Solve Time: 0.173894 s + compositionalMultiphaseFlow: Max pressure change: 285.765 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.042 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.459640983110134e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.82e-04 ) + Last LinSolve(iter,res) = ( 2, 7.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98143e+06, 1.02696e+07, 1.06916e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05246e+06, -869526 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.32e+09 s, dt: 4320000 s, Cycle: 587 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00836472 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601479 s | Solve Time: 0.17368 s + compositionalMultiphaseFlow: Max pressure change: 286.306 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.105 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4296678746704714e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.36e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98155e+06, 1.02696e+07, 1.06917e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0523e+06, -869392 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.32e+09 s, dt: 4320000 s, Cycle: 588 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00835949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600669 s | Solve Time: 0.174426 s + compositionalMultiphaseFlow: Max pressure change: 286.121 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.122 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3670830395783327e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.36e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98168e+06, 1.02696e+07, 1.06919e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05215e+06, -869262 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.32e+09 s, dt: 4320000 s, Cycle: 589 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00835644 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607858 s | Solve Time: 0.174261 s + compositionalMultiphaseFlow: Max pressure change: 285.936 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.093 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6946083775403196e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.36e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9818e+06, 1.02697e+07, 1.0692e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05199e+06, -869137 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.33e+09 s, dt: 4320000 s, Cycle: 590 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00834774 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603337 s | Solve Time: 0.173823 s + compositionalMultiphaseFlow: Max pressure change: 285.754 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.019 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.574862244530962e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.87e-04 ) + Last LinSolve(iter,res) = ( 2, 8.35e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98192e+06, 1.02697e+07, 1.06921e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05184e+06, -869015 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.33e+09 s, dt: 3000000 s, Cycle: 591 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.15e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.15e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00564248 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599453 s | Solve Time: 0.173918 s + compositionalMultiphaseFlow: Max pressure change: 200.851 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29.844 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.2107564196248717e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.93e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.93e-05 ) + Last LinSolve(iter,res) = ( 2, 5.64e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.982e+06, 1.02697e+07, 1.06922e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05169e+06, -868898 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69923e+11 } } mol +Time: 2.34e+09 s, dt: 4320000 s, Cycle: 592 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00825663 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.597832 s | Solve Time: 0.173727 s + compositionalMultiphaseFlow: Max pressure change: 283.385 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.874 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.186549634492941e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.86e-04 ) + Last LinSolve(iter,res) = ( 2, 8.26e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98212e+06, 1.02697e+07, 1.06923e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05158e+06, -868825 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.34e+09 s, dt: 4320000 s, Cycle: 593 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00829931 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60161 s | Solve Time: 0.17389 s + compositionalMultiphaseFlow: Max pressure change: 285.530 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.784 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.869941722050129e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.85e-04 ) + Last LinSolve(iter,res) = ( 2, 8.30e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98225e+06, 1.02697e+07, 1.06924e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05143e+06, -868707 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.34e+09 s, dt: 4320000 s, Cycle: 594 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00831059 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601124 s | Solve Time: 0.174145 s + compositionalMultiphaseFlow: Max pressure change: 285.819 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.712 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4914043617041415e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.85e-04 ) + Last LinSolve(iter,res) = ( 2, 8.31e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98237e+06, 1.02698e+07, 1.06925e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05127e+06, -868600 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.35e+09 s, dt: 4320000 s, Cycle: 595 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00822347 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599549 s | Solve Time: 0.172463 s + compositionalMultiphaseFlow: Max pressure change: 285.408 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.756 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9238720988811195e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 8.22e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98249e+06, 1.02698e+07, 1.06926e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05112e+06, -868497 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.35e+09 s, dt: 4320000 s, Cycle: 596 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00821548 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606117 s | Solve Time: 0.174009 s + compositionalMultiphaseFlow: Max pressure change: 285.514 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.800 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4100897022538703e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.22e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98261e+06, 1.02698e+07, 1.06927e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05098e+06, -868398 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.36e+09 s, dt: 4320000 s, Cycle: 597 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00820516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602963 s | Solve Time: 0.174052 s + compositionalMultiphaseFlow: Max pressure change: 285.528 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.008 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4447758284473764e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.82e-04 ) + Last LinSolve(iter,res) = ( 2, 8.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98273e+06, 1.02698e+07, 1.06928e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05084e+06, -868303 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.36e+09 s, dt: 4320000 s, Cycle: 598 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00819419 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598833 s | Solve Time: 0.174456 s + compositionalMultiphaseFlow: Max pressure change: 285.506 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.166 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.667599238170837e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.19e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98285e+06, 1.02698e+07, 1.06929e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05071e+06, -868211 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.37e+09 s, dt: 1320000 s, Cycle: 599 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.20e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0024416 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606559 s | Solve Time: 0.17416 s + compositionalMultiphaseFlow: Max pressure change: 91.583 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13.241 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.552834451250099e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-05 ) + Last LinSolve(iter,res) = ( 2, 2.44e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98288e+06, 1.02698e+07, 1.06929e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05057e+06, -868123 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.37e+09 s, dt: 2640000 s, Cycle: 600 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00489808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599572 s | Solve Time: 0.174608 s + compositionalMultiphaseFlow: Max pressure change: 174.114 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.472 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7383903138101786e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.85e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.85e-05 ) + Last LinSolve(iter,res) = ( 2, 4.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98295e+06, 1.02699e+07, 1.06929e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05053e+06, -868110 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69922e+11 } } mol +Time: 2.37e+09 s, dt: 4320000 s, Cycle: 601 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00801954 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600424 s | Solve Time: 0.174703 s + compositionalMultiphaseFlow: Max pressure change: 282.176 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.334 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.902505175568116e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 2, 8.02e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98307e+06, 1.02699e+07, 1.0693e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05044e+06, -868053 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.37e+09 s, dt: 4320000 s, Cycle: 602 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00812107 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604223 s | Solve Time: 0.175696 s + compositionalMultiphaseFlow: Max pressure change: 285.066 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.360 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.327773341859185e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 8.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98319e+06, 1.02699e+07, 1.06931e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0503e+06, -867963 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.38e+09 s, dt: 4320000 s, Cycle: 603 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00814391 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60501 s | Solve Time: 0.174097 s + compositionalMultiphaseFlow: Max pressure change: 285.322 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.345 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2751082706662373e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98331e+06, 1.02699e+07, 1.06932e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05017e+06, -867886 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.38e+09 s, dt: 4320000 s, Cycle: 604 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00813672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598643 s | Solve Time: 0.174381 s + compositionalMultiphaseFlow: Max pressure change: 285.236 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.405 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.384832860080621e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.82e-04 ) + Last LinSolve(iter,res) = ( 2, 8.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98343e+06, 1.02699e+07, 1.06933e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.05003e+06, -867812 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.39e+09 s, dt: 4320000 s, Cycle: 605 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00812656 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599113 s | Solve Time: 0.173846 s + compositionalMultiphaseFlow: Max pressure change: 285.116 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.583 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5973985862126625e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98355e+06, 1.027e+07, 1.06933e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04989e+06, -867742 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.39e+09 s, dt: 4320000 s, Cycle: 606 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00811533 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599248 s | Solve Time: 0.172549 s + compositionalMultiphaseFlow: Max pressure change: 284.990 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.710 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.574666029264705e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98366e+06, 1.027e+07, 1.06934e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04975e+06, -867675 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.40e+09 s, dt: 3000000 s, Cycle: 607 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.36e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00549905 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605043 s | Solve Time: 0.174158 s + compositionalMultiphaseFlow: Max pressure change: 200.467 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 30.422 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.237073336936902e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.76e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.76e-05 ) + Last LinSolve(iter,res) = ( 2, 5.50e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98374e+06, 1.027e+07, 1.06934e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04962e+06, -867612 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.40e+09 s, dt: 4320000 s, Cycle: 608 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00801985 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599977 s | Solve Time: 0.174427 s + compositionalMultiphaseFlow: Max pressure change: 282.576 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.815 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3040883484769523e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.02e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98386e+06, 1.027e+07, 1.06935e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04952e+06, -867577 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.40e+09 s, dt: 4320000 s, Cycle: 609 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00805558 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603095 s | Solve Time: 0.172049 s + compositionalMultiphaseFlow: Max pressure change: 284.364 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.817 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.3760794576332955e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98398e+06, 1.027e+07, 1.06935e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04938e+06, -867513 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.41e+09 s, dt: 4320000 s, Cycle: 610 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00806543 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602078 s | Solve Time: 0.174135 s + compositionalMultiphaseFlow: Max pressure change: 284.430 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.768 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.19421672054132e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 8.07e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98409e+06, 1.027e+07, 1.06936e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04925e+06, -867459 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69921e+11 } } mol +Time: 2.41e+09 s, dt: 4320000 s, Cycle: 611 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00805502 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601741 s | Solve Time: 0.172064 s + compositionalMultiphaseFlow: Max pressure change: 284.233 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.692 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2641353181196422e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 8.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98421e+06, 1.02701e+07, 1.06936e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04911e+06, -867408 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.42e+09 s, dt: 4320000 s, Cycle: 612 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00804188 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602499 s | Solve Time: 0.1748 s + compositionalMultiphaseFlow: Max pressure change: 284.004 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.799 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2862723036976007e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 8.04e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98432e+06, 1.02701e+07, 1.06937e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04898e+06, -867361 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.42e+09 s, dt: 4320000 s, Cycle: 613 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.07e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00802822 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600926 s | Solve Time: 0.174667 s + compositionalMultiphaseFlow: Max pressure change: 283.766 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.918 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1279152362385645e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.84e-04 ) + Last LinSolve(iter,res) = ( 2, 8.03e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98444e+06, 1.02701e+07, 1.06937e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04884e+06, -867316 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.42e+09 s, dt: 4320000 s, Cycle: 614 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.07e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00801451 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602307 s | Solve Time: 0.174296 s + compositionalMultiphaseFlow: Max pressure change: 283.510 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.985 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.2018277234803207e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.83e-04 ) + Last LinSolve(iter,res) = ( 2, 8.01e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98455e+06, 1.02701e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04871e+06, -867275 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.43e+09 s, dt: 1320000 s, Cycle: 615 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.25e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00239582 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601189 s | Solve Time: 0.174185 s + compositionalMultiphaseFlow: Max pressure change: 90.664 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13.454 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.8022238504928936e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.63e-05 ) + Last LinSolve(iter,res) = ( 2, 2.40e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98459e+06, 1.02701e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04857e+06, -867238 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.43e+09 s, dt: 2640000 s, Cycle: 616 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.49e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00473798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602004 s | Solve Time: 0.175441 s + compositionalMultiphaseFlow: Max pressure change: 173.592 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.896 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8044004871375918e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.92e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.92e-05 ) + Last LinSolve(iter,res) = ( 2, 4.74e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98466e+06, 1.02701e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04853e+06, -867240 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.43e+09 s, dt: 4320000 s, Cycle: 617 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.007789 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599847 s | Solve Time: 0.174222 s + compositionalMultiphaseFlow: Max pressure change: 281.311 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.984 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.039653974108326e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 7.79e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98477e+06, 1.02701e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04845e+06, -867214 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.44e+09 s, dt: 4320000 s, Cycle: 618 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00788856 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603084 s | Solve Time: 0.174062 s + compositionalMultiphaseFlow: Max pressure change: 283.187 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.924 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1038609643309059e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 7.89e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98489e+06, 1.02702e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04831e+06, -867174 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.44e+09 s, dt: 4320000 s, Cycle: 619 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00795616 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606351 s | Solve Time: 0.174292 s + compositionalMultiphaseFlow: Max pressure change: 283.235 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.822 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0981238602058028e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.81e-04 ) + Last LinSolve(iter,res) = ( 2, 7.96e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.985e+06, 1.02702e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04818e+06, -867145 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.45e+09 s, dt: 4320000 s, Cycle: 620 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00794599 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607148 s | Solve Time: 0.172921 s + compositionalMultiphaseFlow: Max pressure change: 282.888 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.715 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0679329015838022e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.80e-04 ) + Last LinSolve(iter,res) = ( 2, 7.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98511e+06, 1.02702e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04804e+06, -867120 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.6992e+11 } } mol +Time: 2.45e+09 s, dt: 4320000 s, Cycle: 621 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00793374 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601801 s | Solve Time: 0.174285 s + compositionalMultiphaseFlow: Max pressure change: 282.821 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.814 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0695392088931897e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.79e-04 ) + Last LinSolve(iter,res) = ( 2, 7.93e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98523e+06, 1.02702e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04791e+06, -867097 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.45e+09 s, dt: 4320000 s, Cycle: 622 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00792363 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600268 s | Solve Time: 0.172219 s + compositionalMultiphaseFlow: Max pressure change: 282.786 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.885 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0575287174029455e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.77e-04 ) + Last LinSolve(iter,res) = ( 2, 7.92e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98534e+06, 1.02702e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04778e+06, -867078 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.46e+09 s, dt: 3000000 s, Cycle: 623 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.36e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.36e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00537622 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601368 s | Solve Time: 0.173959 s + compositionalMultiphaseFlow: Max pressure change: 198.609 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 30.506 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.286746547259689e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.47e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.47e-05 ) + Last LinSolve(iter,res) = ( 2, 5.38e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98542e+06, 1.02702e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04764e+06, -867061 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.46e+09 s, dt: 4320000 s, Cycle: 624 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.06e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00782778 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601921 s | Solve Time: 0.174163 s + compositionalMultiphaseFlow: Max pressure change: 280.929 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.885 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.3230675303697055e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.83e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98553e+06, 1.02703e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04755e+06, -867057 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99818e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.47e+09 s, dt: 4320000 s, Cycle: 625 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0078109 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601694 s | Solve Time: 0.173749 s + compositionalMultiphaseFlow: Max pressure change: 282.456 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.819 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0331729533307197e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.81e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98564e+06, 1.02703e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04742e+06, -867038 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.47e+09 s, dt: 4320000 s, Cycle: 626 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00782002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601082 s | Solve Time: 0.174044 s + compositionalMultiphaseFlow: Max pressure change: 282.462 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.703 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0385202115225098e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.75e-04 ) + Last LinSolve(iter,res) = ( 2, 7.82e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98575e+06, 1.02703e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04729e+06, -867029 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.47e+09 s, dt: 4320000 s, Cycle: 627 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00780918 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.598635 s | Solve Time: 0.172712 s + compositionalMultiphaseFlow: Max pressure change: 282.308 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.543 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.019020002297367e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.76e-04 ) + Last LinSolve(iter,res) = ( 2, 7.81e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98586e+06, 1.02703e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04716e+06, -867023 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.48e+09 s, dt: 4320000 s, Cycle: 628 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00763403 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602026 s | Solve Time: 0.174178 s + compositionalMultiphaseFlow: Max pressure change: 282.285 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.336 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0318508209271613e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.73e-04 ) + Last LinSolve(iter,res) = ( 2, 7.63e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98597e+06, 1.02703e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04702e+06, -867019 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69919e+11 } } mol +Time: 2.48e+09 s, dt: 4320000 s, Cycle: 629 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00762236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599827 s | Solve Time: 0.174123 s + compositionalMultiphaseFlow: Max pressure change: 282.101 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.558 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0003706813209732e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.62e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98608e+06, 1.02703e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04689e+06, -867018 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.49e+09 s, dt: 4320000 s, Cycle: 630 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00761372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60002 s | Solve Time: 0.174873 s + compositionalMultiphaseFlow: Max pressure change: 281.823 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.574 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.004779031672399e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.61e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98619e+06, 1.02704e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04676e+06, -867020 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.49e+09 s, dt: 1320000 s, Cycle: 631 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.21e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.21e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00233599 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607399 s | Solve Time: 0.172119 s + compositionalMultiphaseFlow: Max pressure change: 89.816 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 13.358 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.713916889638071e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.54e-05 ) + Last LinSolve(iter,res) = ( 2, 2.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98623e+06, 1.02704e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04663e+06, -867024 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.49e+09 s, dt: 2640000 s, Cycle: 632 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0046232 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602564 s | Solve Time: 0.173737 s + compositionalMultiphaseFlow: Max pressure change: 172.359 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.651 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7751511199870507e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.68e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.68e-05 ) + Last LinSolve(iter,res) = ( 2, 4.62e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98629e+06, 1.02704e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04659e+06, -867037 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.50e+09 s, dt: 4320000 s, Cycle: 633 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.05e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00743851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601004 s | Solve Time: 0.17406 s + compositionalMultiphaseFlow: Max pressure change: 278.803 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.478 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.950569625543743e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.73e-04 ) + Last LinSolve(iter,res) = ( 2, 7.44e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9864e+06, 1.02704e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04651e+06, -867037 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.50e+09 s, dt: 4320000 s, Cycle: 634 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00752782 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605992 s | Solve Time: 0.174351 s + compositionalMultiphaseFlow: Max pressure change: 281.117 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.362 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9837239439990384e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.73e-04 ) + Last LinSolve(iter,res) = ( 2, 7.53e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98651e+06, 1.02704e+07, 1.0694e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04638e+06, -867038 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.50e+09 s, dt: 4320000 s, Cycle: 635 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00754888 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601586 s | Solve Time: 0.174362 s + compositionalMultiphaseFlow: Max pressure change: 281.535 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.192 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9485321556267365e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.55e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98662e+06, 1.02704e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04626e+06, -867049 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.51e+09 s, dt: 4320000 s, Cycle: 636 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00746489 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599692 s | Solve Time: 0.174336 s + compositionalMultiphaseFlow: Max pressure change: 281.505 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.980 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.935853671808374e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.46e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98673e+06, 1.02704e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04613e+06, -867063 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.51e+09 s, dt: 4320000 s, Cycle: 637 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00744866 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601619 s | Solve Time: 0.177425 s + compositionalMultiphaseFlow: Max pressure change: 281.520 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.900 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9466325384964733e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.74e-04 ) + Last LinSolve(iter,res) = ( 2, 7.45e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98684e+06, 1.02705e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.046e+06, -867079 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69918e+11 } } mol +Time: 2.52e+09 s, dt: 4320000 s, Cycle: 638 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.04e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00743231 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607004 s | Solve Time: 0.174789 s + compositionalMultiphaseFlow: Max pressure change: 281.524 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.992 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.945086784971295e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.73e-04 ) + Last LinSolve(iter,res) = ( 2, 7.43e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98694e+06, 1.02705e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04587e+06, -867097 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.52e+09 s, dt: 3000000 s, Cycle: 639 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.20e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.20e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00522527 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602867 s | Solve Time: 0.174193 s + compositionalMultiphaseFlow: Max pressure change: 197.821 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29.913 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.183143379104081e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.36e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.36e-05 ) + Last LinSolve(iter,res) = ( 2, 5.23e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98702e+06, 1.02705e+07, 1.06939e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04574e+06, -867118 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.52e+09 s, dt: 4320000 s, Cycle: 640 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00733796 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600283 s | Solve Time: 0.174229 s + compositionalMultiphaseFlow: Max pressure change: 279.504 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 43.028 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.203622269021267e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.72e-04 ) + Last LinSolve(iter,res) = ( 2, 7.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98713e+06, 1.02705e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04565e+06, -867139 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.53e+09 s, dt: 4320000 s, Cycle: 641 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.03e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00736011 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602441 s | Solve Time: 0.174154 s + compositionalMultiphaseFlow: Max pressure change: 281.160 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.846 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9565251752062807e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.71e-04 ) + Last LinSolve(iter,res) = ( 2, 7.36e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98723e+06, 1.02705e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04552e+06, -867157 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.53e+09 s, dt: 4320000 s, Cycle: 642 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.007366 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601566 s | Solve Time: 0.174568 s + compositionalMultiphaseFlow: Max pressure change: 281.325 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.691 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9086236169307824e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.71e-04 ) + Last LinSolve(iter,res) = ( 2, 7.37e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98734e+06, 1.02705e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0454e+06, -867184 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.54e+09 s, dt: 4320000 s, Cycle: 643 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00735361 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600216 s | Solve Time: 0.175301 s + compositionalMultiphaseFlow: Max pressure change: 281.264 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.491 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9536075468451486e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.70e-04 ) + Last LinSolve(iter,res) = ( 2, 7.35e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98744e+06, 1.02705e+07, 1.06938e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04527e+06, -867212 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.54e+09 s, dt: 4320000 s, Cycle: 644 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00733796 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603299 s | Solve Time: 0.174335 s + compositionalMultiphaseFlow: Max pressure change: 281.160 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.329 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9462836697847763e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.69e-04 ) + Last LinSolve(iter,res) = ( 2, 7.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98755e+06, 1.02706e+07, 1.06937e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04515e+06, -867243 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.55e+09 s, dt: 4320000 s, Cycle: 645 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00732264 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606451 s | Solve Time: 0.174235 s + compositionalMultiphaseFlow: Max pressure change: 281.033 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.413 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9460126732262495e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.67e-04 ) + Last LinSolve(iter,res) = ( 2, 7.32e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98765e+06, 1.02706e+07, 1.06937e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04502e+06, -867276 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.55e+09 s, dt: 4320000 s, Cycle: 646 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00730732 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599861 s | Solve Time: 0.174132 s + compositionalMultiphaseFlow: Max pressure change: 280.891 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.445 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9455191657691273e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.66e-04 ) + Last LinSolve(iter,res) = ( 2, 7.31e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98776e+06, 1.02706e+07, 1.06937e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04489e+06, -867311 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.56e+09 s, dt: 1320000 s, Cycle: 647 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.12e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.12e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00226384 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604467 s | Solve Time: 0.17442 s + compositionalMultiphaseFlow: Max pressure change: 89.527 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.982 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.438637793675483e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-05 ) + Last LinSolve(iter,res) = ( 2, 2.26e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98779e+06, 1.02706e+07, 1.06936e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04477e+06, -867348 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.56e+09 s, dt: 2640000 s, Cycle: 648 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.22e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00449908 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602908 s | Solve Time: 0.173411 s + compositionalMultiphaseFlow: Max pressure change: 171.727 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25.945 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6885516670450684e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.22e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.22e-05 ) + Last LinSolve(iter,res) = ( 2, 4.50e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98786e+06, 1.02706e+07, 1.06936e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04473e+06, -867369 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.56e+09 s, dt: 4320000 s, Cycle: 649 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00713645 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603614 s | Solve Time: 0.173378 s + compositionalMultiphaseFlow: Max pressure change: 277.553 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.378 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.7686785308022053e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-04 ) + Last LinSolve(iter,res) = ( 2, 7.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98796e+06, 1.02706e+07, 1.06936e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04465e+06, -867390 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.56e+09 s, dt: 4320000 s, Cycle: 650 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.02e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00721881 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603868 s | Solve Time: 0.175167 s + compositionalMultiphaseFlow: Max pressure change: 279.936 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 42.269 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9587949162680474e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-04 ) + Last LinSolve(iter,res) = ( 2, 7.22e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98806e+06, 1.02706e+07, 1.06935e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04453e+06, -867423 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 2.57e+09 s, dt: 4320000 s, Cycle: 651 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00723881 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.608418 s | Solve Time: 0.174538 s + compositionalMultiphaseFlow: Max pressure change: 280.083 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.999 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.977514423323612e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.61e-04 ) + Last LinSolve(iter,res) = ( 2, 7.24e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98817e+06, 1.02707e+07, 1.06935e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04441e+06, -867465 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.57e+09 s, dt: 4320000 s, Cycle: 652 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00722958 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605135 s | Solve Time: 0.174868 s + compositionalMultiphaseFlow: Max pressure change: 279.910 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.744 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9659494598922578e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.59e-04 ) + Last LinSolve(iter,res) = ( 2, 7.23e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98827e+06, 1.02707e+07, 1.06934e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04428e+06, -867509 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.58e+09 s, dt: 4320000 s, Cycle: 653 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00721206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601001 s | Solve Time: 0.174601 s + compositionalMultiphaseFlow: Max pressure change: 279.678 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.770 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9290029995566726e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 7.21e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98837e+06, 1.02707e+07, 1.06934e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04416e+06, -867555 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.58e+09 s, dt: 4320000 s, Cycle: 654 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.01e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00720443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60631 s | Solve Time: 0.174352 s + compositionalMultiphaseFlow: Max pressure change: 279.315 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.800 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9261518635627084e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.57e-04 ) + Last LinSolve(iter,res) = ( 2, 7.20e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98847e+06, 1.02707e+07, 1.06933e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04404e+06, -867603 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.58e+09 s, dt: 3000000 s, Cycle: 655 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.99e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.99e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00509102 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602445 s | Solve Time: 0.174428 s + compositionalMultiphaseFlow: Max pressure change: 196.221 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 29.045 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0008649533064258e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.58e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.58e-05 ) + Last LinSolve(iter,res) = ( 2, 5.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98855e+06, 1.02707e+07, 1.06933e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04392e+06, -867652 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.59e+09 s, dt: 4320000 s, Cycle: 656 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00711757 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60366 s | Solve Time: 0.1747 s + compositionalMultiphaseFlow: Max pressure change: 276.968 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.735 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0129129942046973e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 7.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98865e+06, 1.02707e+07, 1.06933e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04383e+06, -867693 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.59e+09 s, dt: 4320000 s, Cycle: 657 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-02 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.00e-02 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00713659 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599273 s | Solve Time: 0.174318 s + compositionalMultiphaseFlow: Max pressure change: 278.356 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.634 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9870666023713568e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.57e-04 ) + Last LinSolve(iter,res) = ( 2, 7.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98875e+06, 1.02707e+07, 1.06932e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04371e+06, -867740 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.60e+09 s, dt: 4320000 s, Cycle: 658 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.95e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00715841 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603215 s | Solve Time: 0.174256 s + compositionalMultiphaseFlow: Max pressure change: 277.969 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.487 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9807640183611142e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 7.16e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98885e+06, 1.02708e+07, 1.06932e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04359e+06, -867793 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.60e+09 s, dt: 4320000 s, Cycle: 659 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.94e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00713861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603409 s | Solve Time: 0.175037 s + compositionalMultiphaseFlow: Max pressure change: 278.263 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.297 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9538563778009888e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 7.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98895e+06, 1.02708e+07, 1.06931e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04347e+06, -867848 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.61e+09 s, dt: 4320000 s, Cycle: 660 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.95e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00712814 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601102 s | Solve Time: 0.17434 s + compositionalMultiphaseFlow: Max pressure change: 277.781 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.153 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9439825349465423e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 7.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98905e+06, 1.02708e+07, 1.0693e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04335e+06, -867905 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.61e+09 s, dt: 4320000 s, Cycle: 661 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.95e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00712023 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601879 s | Solve Time: 0.174328 s + compositionalMultiphaseFlow: Max pressure change: 277.375 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.197 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9720126476219235e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.58e-04 ) + Last LinSolve(iter,res) = ( 2, 7.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98915e+06, 1.02708e+07, 1.0693e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04323e+06, -867964 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 2.61e+09 s, dt: 4320000 s, Cycle: 662 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.93e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00711294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603161 s | Solve Time: 0.174898 s + compositionalMultiphaseFlow: Max pressure change: 276.967 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.190 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9918320182110705e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.57e-04 ) + Last LinSolve(iter,res) = ( 2, 7.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98925e+06, 1.02708e+07, 1.06929e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04311e+06, -868023 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.62e+09 s, dt: 1320000 s, Cycle: 663 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 3.03e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00219237 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600097 s | Solve Time: 0.174619 s + compositionalMultiphaseFlow: Max pressure change: 87.991 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.628 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 5.125131329442034e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.38e-05 ) + Last LinSolve(iter,res) = ( 2, 2.19e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98928e+06, 1.02708e+07, 1.06929e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04299e+06, -868085 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.62e+09 s, dt: 2640000 s, Cycle: 664 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.05e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.05e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00444413 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604449 s | Solve Time: 0.174238 s + compositionalMultiphaseFlow: Max pressure change: 169.100 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25.184 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5893675268108254e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.04e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.04e-05 ) + Last LinSolve(iter,res) = ( 2, 4.44e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98934e+06, 1.02708e+07, 1.06929e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04295e+06, -868113 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.62e+09 s, dt: 4320000 s, Cycle: 665 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.87e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.87e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00695072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600601 s | Solve Time: 0.174255 s + compositionalMultiphaseFlow: Max pressure change: 273.445 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 41.047 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.5296552191033115e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.55e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98944e+06, 1.02709e+07, 1.06928e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04288e+06, -868149 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.63e+09 s, dt: 4320000 s, Cycle: 666 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.82e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.82e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00703001 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601128 s | Solve Time: 0.174203 s + compositionalMultiphaseFlow: Max pressure change: 275.390 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.912 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9696853925665891e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.55e-04 ) + Last LinSolve(iter,res) = ( 2, 7.03e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98954e+06, 1.02709e+07, 1.06927e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04276e+06, -868206 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.63e+09 s, dt: 4320000 s, Cycle: 667 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.77e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00705226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.6 s | Solve Time: 0.174465 s + compositionalMultiphaseFlow: Max pressure change: 275.232 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.723 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.947506449440084e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.56e-04 ) + Last LinSolve(iter,res) = ( 2, 7.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98964e+06, 1.02709e+07, 1.06927e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04264e+06, -868271 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.64e+09 s, dt: 4320000 s, Cycle: 668 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00704612 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59963 s | Solve Time: 0.174088 s + compositionalMultiphaseFlow: Max pressure change: 274.795 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.492 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9769551196091584e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.55e-04 ) + Last LinSolve(iter,res) = ( 2, 7.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98974e+06, 1.02709e+07, 1.06926e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04253e+06, -868337 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.64e+09 s, dt: 4320000 s, Cycle: 669 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00699813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.608279 s | Solve Time: 0.17437 s + compositionalMultiphaseFlow: Max pressure change: 274.538 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.453 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.006892563244378e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.55e-04 ) + Last LinSolve(iter,res) = ( 2, 7.00e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98983e+06, 1.02709e+07, 1.06925e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04241e+06, -868405 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.64e+09 s, dt: 4320000 s, Cycle: 670 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.77e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00698426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604785 s | Solve Time: 0.17452 s + compositionalMultiphaseFlow: Max pressure change: 273.887 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.475 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9920889582358825e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.54e-04 ) + Last LinSolve(iter,res) = ( 2, 6.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.98993e+06, 1.02709e+07, 1.06925e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04229e+06, -868474 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.65e+09 s, dt: 3000000 s, Cycle: 671 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.77e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.77e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00497378 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606809 s | Solve Time: 0.17427 s + compositionalMultiphaseFlow: Max pressure change: 191.767 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 28.128 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.834474920221375e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.36e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.36e-05 ) + Last LinSolve(iter,res) = ( 2, 4.97e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99e+06, 1.02709e+07, 1.06924e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04218e+06, -868544 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.65e+09 s, dt: 4320000 s, Cycle: 672 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.73e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.73e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00693343 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606822 s | Solve Time: 0.174171 s + compositionalMultiphaseFlow: Max pressure change: 271.074 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.399 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8195893206905964e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 6.93e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99009e+06, 1.0271e+07, 1.06923e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0421e+06, -868598 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.66e+09 s, dt: 4320000 s, Cycle: 673 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.69e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00695144 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599326 s | Solve Time: 0.173894 s + compositionalMultiphaseFlow: Max pressure change: 272.062 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.295 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9463246236917087e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99019e+06, 1.0271e+07, 1.06923e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04198e+06, -868665 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.66e+09 s, dt: 4320000 s, Cycle: 674 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.64e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00704844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603347 s | Solve Time: 0.174629 s + compositionalMultiphaseFlow: Max pressure change: 271.456 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 40.146 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9873955592331072e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99029e+06, 1.0271e+07, 1.06922e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04187e+06, -868738 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.66e+09 s, dt: 4320000 s, Cycle: 675 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.58e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.58e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00704574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601172 s | Solve Time: 0.174143 s + compositionalMultiphaseFlow: Max pressure change: 271.039 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.957 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9923222294160325e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99038e+06, 1.0271e+07, 1.06921e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04175e+06, -868812 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.67e+09 s, dt: 4320000 s, Cycle: 676 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.59e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00703701 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602666 s | Solve Time: 0.174796 s + compositionalMultiphaseFlow: Max pressure change: 270.481 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.730 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0069782458165264e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.04e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99048e+06, 1.0271e+07, 1.0692e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04164e+06, -868888 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.67e+09 s, dt: 4320000 s, Cycle: 677 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.59e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00703277 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.608219 s | Solve Time: 0.174646 s + compositionalMultiphaseFlow: Max pressure change: 269.815 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.692 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0004790901584357e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.03e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99057e+06, 1.0271e+07, 1.0692e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04152e+06, -868964 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.68e+09 s, dt: 4320000 s, Cycle: 678 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.58e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.58e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00702268 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600432 s | Solve Time: 0.173912 s + compositionalMultiphaseFlow: Max pressure change: 269.180 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.695 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9679641127812175e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.02e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99067e+06, 1.0271e+07, 1.06919e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04141e+06, -869041 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.68e+09 s, dt: 1320000 s, Cycle: 679 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.92e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00215496 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602252 s | Solve Time: 0.174143 s + compositionalMultiphaseFlow: Max pressure change: 85.523 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 12.137 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.758109707903024e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.33e-05 ) + Last LinSolve(iter,res) = ( 2, 2.15e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99069e+06, 1.0271e+07, 1.06919e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0413e+06, -869119 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.68e+09 s, dt: 2640000 s, Cycle: 680 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00433534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.609352 s | Solve Time: 0.174127 s + compositionalMultiphaseFlow: Max pressure change: 164.255 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.250 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.474143940360939e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.72e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.72e-05 ) + Last LinSolve(iter,res) = ( 2, 4.34e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99075e+06, 1.02711e+07, 1.06918e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04126e+06, -869152 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.69e+09 s, dt: 4320000 s, Cycle: 681 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.59e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.59e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00687084 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603345 s | Solve Time: 0.174024 s + compositionalMultiphaseFlow: Max pressure change: 265.248 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.595 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.287378462446533e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.87e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99085e+06, 1.02711e+07, 1.06917e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04119e+06, -869199 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.69e+09 s, dt: 4320000 s, Cycle: 682 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00695004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603409 s | Solve Time: 0.173892 s + compositionalMultiphaseFlow: Max pressure change: 266.855 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.478 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.012743373080994e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99094e+06, 1.02711e+07, 1.06917e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04108e+06, -869272 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.69e+09 s, dt: 4320000 s, Cycle: 683 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00696883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602837 s | Solve Time: 0.173907 s + compositionalMultiphaseFlow: Max pressure change: 266.500 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.319 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9940719253597194e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.97e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99103e+06, 1.02711e+07, 1.06916e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04097e+06, -869352 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.70e+09 s, dt: 4320000 s, Cycle: 684 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0069708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604133 s | Solve Time: 0.173924 s + compositionalMultiphaseFlow: Max pressure change: 265.732 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.120 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.006777650720437e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.97e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99113e+06, 1.02711e+07, 1.06915e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04086e+06, -869433 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.70e+09 s, dt: 4320000 s, Cycle: 685 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00696049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603972 s | Solve Time: 0.174148 s + compositionalMultiphaseFlow: Max pressure change: 265.048 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.970 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9965364650431638e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.96e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99122e+06, 1.02711e+07, 1.06914e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04075e+06, -869516 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.71e+09 s, dt: 4320000 s, Cycle: 686 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0069525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600799 s | Solve Time: 0.173765 s + compositionalMultiphaseFlow: Max pressure change: 264.269 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.097 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9598365286199737e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99131e+06, 1.02712e+07, 1.06913e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04064e+06, -869599 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.71e+09 s, dt: 3000000 s, Cycle: 687 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00484317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604528 s | Solve Time: 0.173944 s + compositionalMultiphaseFlow: Max pressure change: 185.210 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.185 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6431259394499307e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.29e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.29e-05 ) + Last LinSolve(iter,res) = ( 2, 4.84e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99137e+06, 1.02712e+07, 1.06913e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04053e+06, -869682 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.71e+09 s, dt: 4320000 s, Cycle: 688 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00688284 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601962 s | Solve Time: 0.174224 s + compositionalMultiphaseFlow: Max pressure change: 261.190 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.181 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6059809536960188e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 6.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99146e+06, 1.02712e+07, 1.06912e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04046e+06, -869746 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.72e+09 s, dt: 4320000 s, Cycle: 689 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00692207 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600017 s | Solve Time: 0.174039 s + compositionalMultiphaseFlow: Max pressure change: 261.781 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.158 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0169306169659507e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.92e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99156e+06, 1.02712e+07, 1.06911e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04035e+06, -869826 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.72e+09 s, dt: 4320000 s, Cycle: 690 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00691677 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602454 s | Solve Time: 0.174096 s + compositionalMultiphaseFlow: Max pressure change: 261.227 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.080 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.010636779292696e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 6.92e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99165e+06, 1.02712e+07, 1.0691e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04024e+06, -869912 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.73e+09 s, dt: 4320000 s, Cycle: 691 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00681534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603106 s | Solve Time: 0.174157 s + compositionalMultiphaseFlow: Max pressure change: 260.573 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.951 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.0069530437538674e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 6.82e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99174e+06, 1.02712e+07, 1.06909e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04014e+06, -869998 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.73e+09 s, dt: 4320000 s, Cycle: 692 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00680835 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603221 s | Solve Time: 0.173977 s + compositionalMultiphaseFlow: Max pressure change: 259.592 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.035 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9790987615397881e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.51e-04 ) + Last LinSolve(iter,res) = ( 2, 6.81e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99183e+06, 1.02712e+07, 1.06908e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.04004e+06, -870085 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.74e+09 s, dt: 4320000 s, Cycle: 693 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00680172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604254 s | Solve Time: 0.174086 s + compositionalMultiphaseFlow: Max pressure change: 258.681 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.113 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9537171469519166e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.80e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99192e+06, 1.02713e+07, 1.06907e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03994e+06, -870172 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.74e+09 s, dt: 4320000 s, Cycle: 694 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.57e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00679563 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602038 s | Solve Time: 0.175053 s + compositionalMultiphaseFlow: Max pressure change: 257.784 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.132 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9248448124287165e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.80e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99201e+06, 1.02713e+07, 1.06907e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03984e+06, -870260 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.74e+09 s, dt: 1320000 s, Cycle: 695 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.92e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00212542 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.608386 s | Solve Time: 0.174967 s + compositionalMultiphaseFlow: Max pressure change: 81.708 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.935 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.5434402945465635e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-05 ) + Last LinSolve(iter,res) = ( 2, 2.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99203e+06, 1.02713e+07, 1.06906e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03974e+06, -870349 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.75e+09 s, dt: 2640000 s, Cycle: 696 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.82e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.82e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00423591 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.610126 s | Solve Time: 0.175111 s + compositionalMultiphaseFlow: Max pressure change: 156.918 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 23.883 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4018820365668816e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.75e-05 ) + Last LinSolve(iter,res) = ( 2, 4.24e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99209e+06, 1.02713e+07, 1.06906e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03971e+06, -870384 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.75e+09 s, dt: 4320000 s, Cycle: 697 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00665274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602755 s | Solve Time: 0.174192 s + compositionalMultiphaseFlow: Max pressure change: 253.882 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.056 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.147213646914615e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.65e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99217e+06, 1.02713e+07, 1.06905e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03965e+06, -870437 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.75e+09 s, dt: 4320000 s, Cycle: 698 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.51e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00673165 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603579 s | Solve Time: 0.174627 s + compositionalMultiphaseFlow: Max pressure change: 254.909 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.950 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9991172905964305e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.73e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99226e+06, 1.02713e+07, 1.06904e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03955e+06, -870521 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.76e+09 s, dt: 4320000 s, Cycle: 699 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.54e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00678589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607042 s | Solve Time: 0.174501 s + compositionalMultiphaseFlow: Max pressure change: 253.891 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.940 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.998753528242858e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.79e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99235e+06, 1.02713e+07, 1.06903e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03945e+06, -870610 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.76e+09 s, dt: 4320000 s, Cycle: 700 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00689315 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606969 s | Solve Time: 0.174633 s + compositionalMultiphaseFlow: Max pressure change: 253.757 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.044 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.946562953047959e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.89e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99244e+06, 1.02713e+07, 1.06902e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03935e+06, -870700 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.77e+09 s, dt: 4320000 s, Cycle: 701 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00690317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599581 s | Solve Time: 0.174299 s + compositionalMultiphaseFlow: Max pressure change: 252.526 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.090 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9302004850008103e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 6.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99252e+06, 1.02714e+07, 1.06901e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03925e+06, -870791 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.77e+09 s, dt: 4320000 s, Cycle: 702 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00690453 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602155 s | Solve Time: 0.17501 s + compositionalMultiphaseFlow: Max pressure change: 251.405 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.079 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9014870256128802e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 6.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99261e+06, 1.02714e+07, 1.069e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03915e+06, -870882 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.77e+09 s, dt: 3000000 s, Cycle: 703 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.61e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.61e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00483427 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606476 s | Solve Time: 0.174708 s + compositionalMultiphaseFlow: Max pressure change: 175.471 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 27.098 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5893576912627836e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.10e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.10e-05 ) + Last LinSolve(iter,res) = ( 2, 4.83e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99267e+06, 1.02714e+07, 1.069e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03905e+06, -870974 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.78e+09 s, dt: 4320000 s, Cycle: 704 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00688178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604508 s | Solve Time: 0.174387 s + compositionalMultiphaseFlow: Max pressure change: 248.121 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.934 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.576434575018993e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 6.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99276e+06, 1.02714e+07, 1.06899e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03899e+06, -871042 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.78e+09 s, dt: 4320000 s, Cycle: 705 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.51e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00681059 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601242 s | Solve Time: 0.174375 s + compositionalMultiphaseFlow: Max pressure change: 247.803 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.827 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9690646202441542e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.44e-04 ) + Last LinSolve(iter,res) = ( 2, 6.81e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99284e+06, 1.02714e+07, 1.06898e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03889e+06, -871130 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.79e+09 s, dt: 4320000 s, Cycle: 706 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.54e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00684281 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603374 s | Solve Time: 0.174605 s + compositionalMultiphaseFlow: Max pressure change: 247.141 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.977 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9712139376348858e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.44e-04 ) + Last LinSolve(iter,res) = ( 2, 6.84e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99293e+06, 1.02714e+07, 1.06897e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03879e+06, -871222 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.79e+09 s, dt: 4320000 s, Cycle: 707 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00697545 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607765 s | Solve Time: 0.17545 s + compositionalMultiphaseFlow: Max pressure change: 246.035 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.068 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9517797189561037e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.45e-04 ) + Last LinSolve(iter,res) = ( 2, 6.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99301e+06, 1.02714e+07, 1.06896e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0387e+06, -871314 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.79e+09 s, dt: 4320000 s, Cycle: 708 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.54e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.54e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00697567 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603139 s | Solve Time: 0.174751 s + compositionalMultiphaseFlow: Max pressure change: 245.262 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.096 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9286884322955444e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 6.98e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9931e+06, 1.02715e+07, 1.06895e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0386e+06, -871407 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.80e+09 s, dt: 4320000 s, Cycle: 709 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00698882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600563 s | Solve Time: 0.174897 s + compositionalMultiphaseFlow: Max pressure change: 244.350 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.068 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8967420634119492e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 6.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99318e+06, 1.02715e+07, 1.06894e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03851e+06, -871500 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.80e+09 s, dt: 4320000 s, Cycle: 710 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00700299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.59994 s | Solve Time: 0.175195 s + compositionalMultiphaseFlow: Max pressure change: 243.169 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.985 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8931769396601794e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.00e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99326e+06, 1.02715e+07, 1.06893e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03841e+06, -871593 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.81e+09 s, dt: 1320000 s, Cycle: 711 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.89e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.89e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00209834 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606201 s | Solve Time: 0.176029 s + compositionalMultiphaseFlow: Max pressure change: 77.257 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.912 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.528274288428946e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.33e-05 ) + Last LinSolve(iter,res) = ( 2, 2.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99329e+06, 1.02715e+07, 1.06893e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03832e+06, -871687 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.81e+09 s, dt: 2640000 s, Cycle: 712 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.78e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.78e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00427574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607027 s | Solve Time: 0.174338 s + compositionalMultiphaseFlow: Max pressure change: 148.156 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 23.754 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3931961780899726e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.58e-05 ) + Last LinSolve(iter,res) = ( 2, 4.28e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99334e+06, 1.02715e+07, 1.06892e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03829e+06, -871723 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.81e+09 s, dt: 4320000 s, Cycle: 713 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00664979 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604287 s | Solve Time: 0.174025 s + compositionalMultiphaseFlow: Max pressure change: 239.614 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.750 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0815178703180734e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 6.65e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99342e+06, 1.02715e+07, 1.06891e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03823e+06, -871780 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.82e+09 s, dt: 4320000 s, Cycle: 714 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00673674 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600696 s | Solve Time: 0.174777 s + compositionalMultiphaseFlow: Max pressure change: 239.975 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.899 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.956873020292349e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.74e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99351e+06, 1.02715e+07, 1.0689e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03814e+06, -871869 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.82e+09 s, dt: 4320000 s, Cycle: 715 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00689651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600236 s | Solve Time: 0.174578 s + compositionalMultiphaseFlow: Max pressure change: 238.764 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.988 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.935712372613807e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99359e+06, 1.02716e+07, 1.06889e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03805e+06, -871962 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.82e+09 s, dt: 4320000 s, Cycle: 716 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.53e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00691713 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600522 s | Solve Time: 0.174832 s + compositionalMultiphaseFlow: Max pressure change: 237.599 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 39.011 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9153447983200067e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 6.92e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99367e+06, 1.02716e+07, 1.06889e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03795e+06, -872056 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.83e+09 s, dt: 4320000 s, Cycle: 717 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.51e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.51e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00693375 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602765 s | Solve Time: 0.175223 s + compositionalMultiphaseFlow: Max pressure change: 236.730 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.972 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8608970098199507e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.93e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99375e+06, 1.02716e+07, 1.06888e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03786e+06, -872151 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.83e+09 s, dt: 4320000 s, Cycle: 718 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00693506 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603143 s | Solve Time: 0.174674 s + compositionalMultiphaseFlow: Max pressure change: 235.415 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.883 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8488562358864868e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99383e+06, 1.02716e+07, 1.06887e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03777e+06, -872245 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.84e+09 s, dt: 3000000 s, Cycle: 719 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.55e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.55e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00484766 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602341 s | Solve Time: 0.17506 s + compositionalMultiphaseFlow: Max pressure change: 164.127 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.927 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.580433926424597e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.32e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.32e-05 ) + Last LinSolve(iter,res) = ( 2, 4.85e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99389e+06, 1.02716e+07, 1.06886e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03768e+06, -872340 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.84e+09 s, dt: 4320000 s, Cycle: 720 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00688262 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603919 s | Solve Time: 0.175052 s + compositionalMultiphaseFlow: Max pressure change: 232.199 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.618 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.5398354326355843e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99397e+06, 1.02716e+07, 1.06885e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03761e+06, -872410 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.84e+09 s, dt: 4320000 s, Cycle: 721 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.45e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00690473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602231 s | Solve Time: 0.174325 s + compositionalMultiphaseFlow: Max pressure change: 232.045 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.724 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.910313025543786e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99405e+06, 1.02716e+07, 1.06884e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03752e+06, -872501 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.85e+09 s, dt: 4320000 s, Cycle: 722 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00693378 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603703 s | Solve Time: 0.174683 s + compositionalMultiphaseFlow: Max pressure change: 230.890 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.818 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.9111294558005198e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.93e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99413e+06, 1.02717e+07, 1.06883e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03743e+06, -872596 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.85e+09 s, dt: 4320000 s, Cycle: 723 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.48e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00693971 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603038 s | Solve Time: 0.17454 s + compositionalMultiphaseFlow: Max pressure change: 229.703 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.851 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8831972037336442e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99421e+06, 1.02717e+07, 1.06882e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03734e+06, -872690 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.86e+09 s, dt: 4320000 s, Cycle: 724 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.47e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00694253 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602172 s | Solve Time: 0.174786 s + compositionalMultiphaseFlow: Max pressure change: 228.435 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.826 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8581806449091687e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99429e+06, 1.02717e+07, 1.06881e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03725e+06, -872785 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.86e+09 s, dt: 4320000 s, Cycle: 725 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.44e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00694702 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602728 s | Solve Time: 0.174365 s + compositionalMultiphaseFlow: Max pressure change: 227.175 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.747 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.822634997372674e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99437e+06, 1.02717e+07, 1.0688e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03717e+06, -872880 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.87e+09 s, dt: 4320000 s, Cycle: 726 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00694899 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605741 s | Solve Time: 0.174927 s + compositionalMultiphaseFlow: Max pressure change: 225.912 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.628 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7748633529546254e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99444e+06, 1.02717e+07, 1.06879e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03708e+06, -872975 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.87e+09 s, dt: 1320000 s, Cycle: 727 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00209414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604362 s | Solve Time: 0.174683 s + compositionalMultiphaseFlow: Max pressure change: 70.851 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.761 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.463383074360117e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.35e-05 ) + Last LinSolve(iter,res) = ( 2, 2.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99447e+06, 1.02717e+07, 1.06879e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03699e+06, -873070 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.87e+09 s, dt: 2640000 s, Cycle: 728 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.71e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.71e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00426082 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60212 s | Solve Time: 0.174481 s + compositionalMultiphaseFlow: Max pressure change: 137.146 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 23.493 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3661709660217625e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.67e-05 ) + Last LinSolve(iter,res) = ( 2, 4.26e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99451e+06, 1.02717e+07, 1.06878e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03696e+06, -873105 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.87e+09 s, dt: 4320000 s, Cycle: 729 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.40e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.40e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00681214 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602319 s | Solve Time: 0.174279 s + compositionalMultiphaseFlow: Max pressure change: 221.262 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.396 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.0339824882430477e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 6.81e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99459e+06, 1.02717e+07, 1.06878e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03691e+06, -873163 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.88e+09 s, dt: 4320000 s, Cycle: 730 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00694298 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599675 s | Solve Time: 0.174775 s + compositionalMultiphaseFlow: Max pressure change: 221.879 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.533 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8644724730787487e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 6.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99467e+06, 1.02718e+07, 1.06877e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03682e+06, -873252 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.88e+09 s, dt: 4320000 s, Cycle: 731 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.44e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00701298 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607541 s | Solve Time: 0.174838 s + compositionalMultiphaseFlow: Max pressure change: 220.839 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.603 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.85948546782555e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.01e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99475e+06, 1.02718e+07, 1.06876e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03674e+06, -873346 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.89e+09 s, dt: 4320000 s, Cycle: 732 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.43e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00705355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601747 s | Solve Time: 0.175262 s + compositionalMultiphaseFlow: Max pressure change: 219.110 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.610 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8391580203225288e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.05e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99482e+06, 1.02718e+07, 1.06875e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03665e+06, -873440 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.89e+09 s, dt: 4320000 s, Cycle: 733 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.41e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.41e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0070305 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603793 s | Solve Time: 0.174622 s + compositionalMultiphaseFlow: Max pressure change: 218.616 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.568 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.8063605333740185e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 7.03e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9949e+06, 1.02718e+07, 1.06874e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03656e+06, -873534 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.90e+09 s, dt: 4320000 s, Cycle: 734 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.38e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.38e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00689959 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606801 s | Solve Time: 0.174698 s + compositionalMultiphaseFlow: Max pressure change: 217.396 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.462 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7586918987788636e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.47e-04 ) + Last LinSolve(iter,res) = ( 2, 6.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99497e+06, 1.02718e+07, 1.06873e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03648e+06, -873629 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.90e+09 s, dt: 3000000 s, Cycle: 735 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.48e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00487635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.611456 s | Solve Time: 0.175052 s + compositionalMultiphaseFlow: Max pressure change: 151.677 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.620 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.531912170034012e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.35e-05 ) + Last LinSolve(iter,res) = ( 2, 4.88e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99502e+06, 1.02718e+07, 1.06872e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03639e+06, -873723 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.90e+09 s, dt: 4320000 s, Cycle: 736 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.30e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.30e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00686722 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607356 s | Solve Time: 0.174637 s + compositionalMultiphaseFlow: Max pressure change: 213.715 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.178 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4827955027451054e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.87e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9951e+06, 1.02718e+07, 1.06871e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03634e+06, -873793 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.91e+09 s, dt: 4320000 s, Cycle: 737 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.33e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.33e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00689523 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606941 s | Solve Time: 0.174604 s + compositionalMultiphaseFlow: Max pressure change: 213.550 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.214 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7735041435429366e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.90e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99517e+06, 1.02719e+07, 1.0687e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03625e+06, -873884 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.91e+09 s, dt: 4320000 s, Cycle: 738 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.35e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00702877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604063 s | Solve Time: 0.174902 s + compositionalMultiphaseFlow: Max pressure change: 211.418 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.330 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7767153059899954e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.03e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99525e+06, 1.02719e+07, 1.06869e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03617e+06, -873977 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.92e+09 s, dt: 4320000 s, Cycle: 739 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.35e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.35e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00694069 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600127 s | Solve Time: 0.174791 s + compositionalMultiphaseFlow: Max pressure change: 211.302 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.386 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.780117306893203e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99532e+06, 1.02719e+07, 1.06868e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03608e+06, -874070 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.92e+09 s, dt: 4320000 s, Cycle: 740 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.34e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00693945 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603874 s | Solve Time: 0.175131 s + compositionalMultiphaseFlow: Max pressure change: 209.762 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.385 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7702371535310846e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.94e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99539e+06, 1.02719e+07, 1.06867e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.036e+06, -874164 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.93e+09 s, dt: 4320000 s, Cycle: 741 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.32e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.32e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00698859 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603561 s | Solve Time: 0.174584 s + compositionalMultiphaseFlow: Max pressure change: 208.002 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.331 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7577338295993172e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 6.99e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99547e+06, 1.02719e+07, 1.06867e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03592e+06, -874257 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.93e+09 s, dt: 4320000 s, Cycle: 742 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.28e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.28e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0070744 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600243 s | Solve Time: 0.174985 s + compositionalMultiphaseFlow: Max pressure change: 206.950 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 38.227 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.7266026752782437e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.07e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99554e+06, 1.02719e+07, 1.06866e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03584e+06, -874350 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.93e+09 s, dt: 1320000 s, Cycle: 743 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.82e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.82e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00209475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605555 s | Solve Time: 0.175018 s + compositionalMultiphaseFlow: Max pressure change: 64.932 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.652 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.36697832573163e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-05 ) + Last LinSolve(iter,res) = ( 2, 2.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99556e+06, 1.02719e+07, 1.06865e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03576e+06, -874443 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.94e+09 s, dt: 2640000 s, Cycle: 744 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.64e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00430561 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604425 s | Solve Time: 0.174858 s + compositionalMultiphaseFlow: Max pressure change: 125.681 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 23.255 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3395199980337225e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.84e-05 ) + Last LinSolve(iter,res) = ( 2, 4.31e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9956e+06, 1.0272e+07, 1.06865e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03573e+06, -874478 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.94e+09 s, dt: 4320000 s, Cycle: 745 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.19e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.19e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00694679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602785 s | Solve Time: 0.174727 s + compositionalMultiphaseFlow: Max pressure change: 202.516 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.881 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.9658328154491542e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99567e+06, 1.0272e+07, 1.06864e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03568e+06, -874534 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.94e+09 s, dt: 4320000 s, Cycle: 746 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.24e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0070414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602311 s | Solve Time: 0.175043 s + compositionalMultiphaseFlow: Max pressure change: 202.668 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.780 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6495046295528226e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.04e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99575e+06, 1.0272e+07, 1.06863e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0356e+06, -874621 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.95e+09 s, dt: 4320000 s, Cycle: 747 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00708827 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60299 s | Solve Time: 0.174727 s + compositionalMultiphaseFlow: Max pressure change: 201.428 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.907 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.688265991450777e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99582e+06, 1.0272e+07, 1.06862e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03552e+06, -874713 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.95e+09 s, dt: 4320000 s, Cycle: 748 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.27e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.27e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00709666 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606759 s | Solve Time: 0.174769 s + compositionalMultiphaseFlow: Max pressure change: 200.158 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.975 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6861766805043032e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99589e+06, 1.0272e+07, 1.06861e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03544e+06, -874804 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.96e+09 s, dt: 4320000 s, Cycle: 749 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.26e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00710257 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602886 s | Solve Time: 0.175569 s + compositionalMultiphaseFlow: Max pressure change: 198.896 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.986 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6969208149753e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99596e+06, 1.0272e+07, 1.0686e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03537e+06, -874896 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.96e+09 s, dt: 4320000 s, Cycle: 750 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.24e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00709985 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603909 s | Solve Time: 0.174389 s + compositionalMultiphaseFlow: Max pressure change: 197.624 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.943 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6712034511812135e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.50e-04 ) + Last LinSolve(iter,res) = ( 2, 7.10e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99603e+06, 1.0272e+07, 1.06859e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03529e+06, -874988 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.96e+09 s, dt: 3000000 s, Cycle: 751 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.39e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.39e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00502049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601055 s | Solve Time: 0.174812 s + compositionalMultiphaseFlow: Max pressure change: 137.928 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 26.274 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.454628368897538e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.22e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.22e-05 ) + Last LinSolve(iter,res) = ( 2, 5.02e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99607e+06, 1.02721e+07, 1.06859e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03521e+06, -875079 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.97e+09 s, dt: 4320000 s, Cycle: 752 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.17e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00706174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604251 s | Solve Time: 0.174733 s + compositionalMultiphaseFlow: Max pressure change: 194.703 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.755 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.430917440898739e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.06e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99614e+06, 1.02721e+07, 1.06858e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03515e+06, -875145 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69914e+11 } } mol +Time: 2.97e+09 s, dt: 4320000 s, Cycle: 753 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.12e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.12e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0070833 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607003 s | Solve Time: 0.175284 s + compositionalMultiphaseFlow: Max pressure change: 194.313 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.583 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.606367494577654e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99621e+06, 1.02721e+07, 1.06857e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03508e+06, -875234 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.98e+09 s, dt: 4320000 s, Cycle: 754 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.06e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.06e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00711262 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603367 s | Solve Time: 0.175059 s + compositionalMultiphaseFlow: Max pressure change: 193.048 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.365 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5326967528483948e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.11e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99628e+06, 1.02721e+07, 1.06856e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.035e+06, -875324 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.98e+09 s, dt: 4320000 s, Cycle: 755 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.05e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.05e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00711594 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604354 s | Solve Time: 0.176269 s + compositionalMultiphaseFlow: Max pressure change: 191.727 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.368 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5404717224054565e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99635e+06, 1.02721e+07, 1.06855e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03492e+06, -875414 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.98e+09 s, dt: 4320000 s, Cycle: 756 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.07e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00712091 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601148 s | Solve Time: 0.174801 s + compositionalMultiphaseFlow: Max pressure change: 190.444 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.459 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5915765061436105e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.49e-04 ) + Last LinSolve(iter,res) = ( 2, 7.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99641e+06, 1.02721e+07, 1.06854e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03485e+06, -875504 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.99e+09 s, dt: 4320000 s, Cycle: 757 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.07e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00712489 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601874 s | Solve Time: 0.17493 s + compositionalMultiphaseFlow: Max pressure change: 189.194 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.495 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5689571764010424e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99648e+06, 1.02721e+07, 1.06853e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03477e+06, -875594 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 2.99e+09 s, dt: 4320000 s, Cycle: 758 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.06e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.06e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00706828 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601821 s | Solve Time: 0.174611 s + compositionalMultiphaseFlow: Max pressure change: 187.806 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.476 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.6233787270003575e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.48e-04 ) + Last LinSolve(iter,res) = ( 2, 7.07e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99655e+06, 1.02722e+07, 1.06852e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0347e+06, -875683 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.00e+09 s, dt: 1320000 s, Cycle: 759 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.76e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.76e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00213623 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606869 s | Solve Time: 0.174581 s + compositionalMultiphaseFlow: Max pressure change: 58.732 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 11.364 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 4.182730614865626e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.39e-05 ) + Last LinSolve(iter,res) = ( 2, 2.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99657e+06, 1.02722e+07, 1.06852e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03462e+06, -875772 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.00e+09 s, dt: 2640000 s, Cycle: 760 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.52e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.52e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0043915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607342 s | Solve Time: 0.174883 s + compositionalMultiphaseFlow: Max pressure change: 114.115 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 22.781 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2829521053303594e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.57e-05 ) + Last LinSolve(iter,res) = ( 2, 4.39e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99661e+06, 1.02722e+07, 1.06851e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0346e+06, -875805 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.00e+09 s, dt: 4320000 s, Cycle: 761 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.03e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 9.03e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00695459 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604955 s | Solve Time: 0.174282 s + compositionalMultiphaseFlow: Max pressure change: 184.244 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.311 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.8833704756037193e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.45e-04 ) + Last LinSolve(iter,res) = ( 2, 6.95e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99667e+06, 1.02722e+07, 1.06851e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03456e+06, -875859 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.01e+09 s, dt: 4320000 s, Cycle: 762 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.99e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.99e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00703601 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607371 s | Solve Time: 0.175027 s + compositionalMultiphaseFlow: Max pressure change: 184.138 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 37.160 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.5703746192308188e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.04e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99674e+06, 1.02722e+07, 1.0685e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03448e+06, -875943 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.01e+09 s, dt: 4320000 s, Cycle: 763 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.94e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0070783 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605028 s | Solve Time: 0.175082 s + compositionalMultiphaseFlow: Max pressure change: 182.941 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.958 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4982252183326494e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9968e+06, 1.02722e+07, 1.06849e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03441e+06, -876030 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.01e+09 s, dt: 4320000 s, Cycle: 764 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.92e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.92e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00712453 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603106 s | Solve Time: 0.17443 s + compositionalMultiphaseFlow: Max pressure change: 181.802 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.713 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4460332731225378e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.46e-04 ) + Last LinSolve(iter,res) = ( 2, 7.12e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99686e+06, 1.02722e+07, 1.06848e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03434e+06, -876118 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.02e+09 s, dt: 4320000 s, Cycle: 765 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.95e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0071295 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60246 s | Solve Time: 0.175106 s + compositionalMultiphaseFlow: Max pressure change: 180.543 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.603 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3993840841663996e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.45e-04 ) + Last LinSolve(iter,res) = ( 2, 7.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99693e+06, 1.02722e+07, 1.06847e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03426e+06, -876205 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.02e+09 s, dt: 4320000 s, Cycle: 766 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.96e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.96e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00713151 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.61038 s | Solve Time: 0.174573 s + compositionalMultiphaseFlow: Max pressure change: 179.290 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.696 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4161501671328125e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.45e-04 ) + Last LinSolve(iter,res) = ( 2, 7.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99699e+06, 1.02723e+07, 1.06846e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03419e+06, -876293 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.03e+09 s, dt: 3000000 s, Cycle: 767 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.23e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00507711 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603617 s | Solve Time: 0.175103 s + compositionalMultiphaseFlow: Max pressure change: 125.054 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 25.459 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.290882896271995e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.07e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 7.07e-05 ) + Last LinSolve(iter,res) = ( 2, 5.08e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99704e+06, 1.02723e+07, 1.06846e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03412e+06, -876379 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.03e+09 s, dt: 4320000 s, Cycle: 768 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.95e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.95e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00713829 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.606059 s | Solve Time: 0.175014 s + compositionalMultiphaseFlow: Max pressure change: 176.267 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.737 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.301847007335489e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 7.14e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9971e+06, 1.02723e+07, 1.06845e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03407e+06, -876442 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.03e+09 s, dt: 4320000 s, Cycle: 769 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.94e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.94e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00715312 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601484 s | Solve Time: 0.175592 s + compositionalMultiphaseFlow: Max pressure change: 175.979 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.694 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4698244021893458e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 7.15e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99716e+06, 1.02723e+07, 1.06844e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.034e+06, -876526 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.04e+09 s, dt: 4320000 s, Cycle: 770 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.91e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.91e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00717771 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605916 s | Solve Time: 0.174883 s + compositionalMultiphaseFlow: Max pressure change: 174.806 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.603 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.46903736175652e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 7.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99722e+06, 1.02723e+07, 1.06843e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03393e+06, -876611 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.04e+09 s, dt: 4320000 s, Cycle: 771 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.86e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.86e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00718395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602484 s | Solve Time: 0.17472 s + compositionalMultiphaseFlow: Max pressure change: 173.582 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.465 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.4344965393320308e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.42e-04 ) + Last LinSolve(iter,res) = ( 2, 7.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99728e+06, 1.02723e+07, 1.06842e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03386e+06, -876697 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.05e+09 s, dt: 4320000 s, Cycle: 772 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.81e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.81e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00717691 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602905 s | Solve Time: 0.174605 s + compositionalMultiphaseFlow: Max pressure change: 172.316 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.284 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.410784726818548e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.42e-04 ) + Last LinSolve(iter,res) = ( 2, 7.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99734e+06, 1.02723e+07, 1.06841e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03379e+06, -876782 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.05e+09 s, dt: 4320000 s, Cycle: 773 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.74e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0073019 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604164 s | Solve Time: 0.174717 s + compositionalMultiphaseFlow: Max pressure change: 171.613 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.068 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3803026166492316e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 7.30e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99741e+06, 1.02724e+07, 1.06841e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03373e+06, -876866 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.06e+09 s, dt: 4320000 s, Cycle: 774 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.72e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00731535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603673 s | Solve Time: 0.174863 s + compositionalMultiphaseFlow: Max pressure change: 170.168 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.826 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.320277215333121e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.43e-04 ) + Last LinSolve(iter,res) = ( 2, 7.32e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99747e+06, 1.02724e+07, 1.0684e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03366e+06, -876950 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.06e+09 s, dt: 1320000 s, Cycle: 775 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.67e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.67e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00208998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.607384 s | Solve Time: 0.174539 s + compositionalMultiphaseFlow: Max pressure change: 52.760 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 10.908 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.876628011267869e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.34e-05 ) + Last LinSolve(iter,res) = ( 2, 2.09e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99748e+06, 1.02724e+07, 1.06839e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03359e+06, -877033 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.06e+09 s, dt: 2640000 s, Cycle: 776 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.34e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00424316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602367 s | Solve Time: 0.174983 s + compositionalMultiphaseFlow: Max pressure change: 105.516 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 21.898 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1752134698728156e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.37e-05 ) + Last LinSolve(iter,res) = ( 2, 4.24e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99752e+06, 1.02724e+07, 1.06839e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03357e+06, -877063 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.06e+09 s, dt: 4320000 s, Cycle: 777 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.75e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.75e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00719878 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.6036 s | Solve Time: 0.174786 s + compositionalMultiphaseFlow: Max pressure change: 167.237 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.985 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.6654312964558002e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 2, 7.20e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99758e+06, 1.02724e+07, 1.06838e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03353e+06, -877114 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.07e+09 s, dt: 4320000 s, Cycle: 778 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.74e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.74e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00727819 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602451 s | Solve Time: 0.174354 s + compositionalMultiphaseFlow: Max pressure change: 166.785 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 36.002 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.307620612900351e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.41e-04 ) + Last LinSolve(iter,res) = ( 2, 7.28e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99764e+06, 1.02724e+07, 1.06837e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03346e+06, -877192 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.07e+09 s, dt: 4320000 s, Cycle: 779 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.72e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.72e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00731692 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604896 s | Solve Time: 0.174887 s + compositionalMultiphaseFlow: Max pressure change: 165.640 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.966 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3134929488511915e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.41e-04 ) + Last LinSolve(iter,res) = ( 2, 7.32e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9977e+06, 1.02724e+07, 1.06836e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03339e+06, -877273 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69915e+11 } } mol +Time: 3.08e+09 s, dt: 4320000 s, Cycle: 780 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.69e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.69e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00728975 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602975 s | Solve Time: 0.174732 s + compositionalMultiphaseFlow: Max pressure change: 166.725 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.881 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3224831874047993e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 2, 7.29e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99776e+06, 1.02724e+07, 1.06836e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03333e+06, -877354 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.08e+09 s, dt: 4320000 s, Cycle: 781 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.65e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.65e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00729228 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602247 s | Solve Time: 0.174979 s + compositionalMultiphaseFlow: Max pressure change: 167.631 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.754 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.3140094490271537e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 2, 7.29e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99781e+06, 1.02725e+07, 1.06835e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03326e+06, -877435 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.09e+09 s, dt: 4320000 s, Cycle: 782 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.60e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.60e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00731557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603961 s | Solve Time: 0.174962 s + compositionalMultiphaseFlow: Max pressure change: 168.386 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.587 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.294864248047034e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.40e-04 ) + Last LinSolve(iter,res) = ( 2, 7.32e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99787e+06, 1.02725e+07, 1.06834e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0332e+06, -877515 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.09e+09 s, dt: 3000000 s, Cycle: 783 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.93e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00480712 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601184 s | Solve Time: 0.174113 s + compositionalMultiphaseFlow: Max pressure change: 115.748 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 24.568 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.188752965204266e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.84e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 6.84e-05 ) + Last LinSolve(iter,res) = ( 2, 4.81e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99791e+06, 1.02725e+07, 1.06833e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03313e+06, -877595 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.09e+09 s, dt: 4320000 s, Cycle: 784 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.49e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.49e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00726894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602716 s | Solve Time: 0.17502 s + compositionalMultiphaseFlow: Max pressure change: 172.715 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 35.209 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.1190187585728992e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.37e-04 ) + Last LinSolve(iter,res) = ( 2, 7.27e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99797e+06, 1.02725e+07, 1.06833e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03309e+06, -877653 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.10e+09 s, dt: 4320000 s, Cycle: 785 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00730898 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.600354 s | Solve Time: 0.173987 s + compositionalMultiphaseFlow: Max pressure change: 169.672 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.947 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.2051906894683384e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.37e-04 ) + Last LinSolve(iter,res) = ( 2, 7.31e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99803e+06, 1.02725e+07, 1.06832e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03302e+06, -877730 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.10e+09 s, dt: 4320000 s, Cycle: 786 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.44e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00730851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603185 s | Solve Time: 0.175425 s + compositionalMultiphaseFlow: Max pressure change: 170.886 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.647 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1517541620431615e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.37e-04 ) + Last LinSolve(iter,res) = ( 2, 7.31e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99808e+06, 1.02725e+07, 1.06831e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03296e+06, -877808 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66544e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.11e+09 s, dt: 4320000 s, Cycle: 787 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.46e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.46e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00732488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603564 s | Solve Time: 0.174779 s + compositionalMultiphaseFlow: Max pressure change: 171.867 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.679 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.1019691503744156e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.37e-04 ) + Last LinSolve(iter,res) = ( 2, 7.32e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99814e+06, 1.02725e+07, 1.0683e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.0329e+06, -877886 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.11e+09 s, dt: 4320000 s, Cycle: 788 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.45e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.45e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00729274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60311 s | Solve Time: 0.175075 s + compositionalMultiphaseFlow: Max pressure change: 172.966 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.706 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0549900464340567e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 7.29e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99819e+06, 1.02726e+07, 1.0683e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03284e+06, -877965 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.11e+09 s, dt: 4320000 s, Cycle: 789 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.44e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.44e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00719327 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601264 s | Solve Time: 0.174768 s + compositionalMultiphaseFlow: Max pressure change: 173.523 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.691 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.079749341048597e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 7.19e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99825e+06, 1.02726e+07, 1.06829e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03277e+06, -878042 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.12e+09 s, dt: 4320000 s, Cycle: 790 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.42e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.42e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00719234 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.604735 s | Solve Time: 0.174261 s + compositionalMultiphaseFlow: Max pressure change: 174.393 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.632 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.089563607115096e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 7.19e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9983e+06, 1.02726e+07, 1.06828e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03271e+06, -878119 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.12e+09 s, dt: 1320000 s, Cycle: 791 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 2.56e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00212574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.603678 s | Solve Time: 0.174395 s + compositionalMultiphaseFlow: Max pressure change: 47.900 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 10.513 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 3.5763967969337784e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.28e-05 ) + Last LinSolve(iter,res) = ( 2, 2.13e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.000 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99832e+06, 1.02726e+07, 1.06828e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03265e+06, -878195 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.12e+09 s, dt: 2640000 s, Cycle: 792 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.10e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0043575 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602309 s | Solve Time: 0.174768 s + compositionalMultiphaseFlow: Max pressure change: 111.829 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 21.045 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0959672221977357e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.05e-05 ) + Last LinSolve(iter,res) = ( 2, 4.36e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99835e+06, 1.02726e+07, 1.06827e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03263e+06, -878223 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.13e+09 s, dt: 4320000 s, Cycle: 793 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.34e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.34e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0071848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.60291 s | Solve Time: 0.174839 s + compositionalMultiphaseFlow: Max pressure change: 178.751 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.412 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.4497739419260256e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.33e-04 ) + Last LinSolve(iter,res) = ( 2, 7.18e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9984e+06, 1.02726e+07, 1.06827e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03259e+06, -878269 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.13e+09 s, dt: 4320000 s, Cycle: 794 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.30e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.30e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00722867 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.599689 s | Solve Time: 0.174842 s + compositionalMultiphaseFlow: Max pressure change: 175.319 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.248 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.113134672214855e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.35e-04 ) + Last LinSolve(iter,res) = ( 2, 7.23e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99846e+06, 1.02726e+07, 1.06826e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03253e+06, -878342 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.14e+09 s, dt: 4320000 s, Cycle: 795 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.24e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.24e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0072038 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.608495 s | Solve Time: 0.174438 s + compositionalMultiphaseFlow: Max pressure change: 176.766 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 34.044 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0764771385396443e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 7.20e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99851e+06, 1.02726e+07, 1.06825e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03247e+06, -878417 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69916e+11 } } mol +Time: 3.14e+09 s, dt: 4320000 s, Cycle: 796 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.17e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.17e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00720475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.601128 s | Solve Time: 0.174375 s + compositionalMultiphaseFlow: Max pressure change: 177.605 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33.805 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.0545603779110735e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.36e-04 ) + Last LinSolve(iter,res) = ( 2, 7.20e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99856e+06, 1.02726e+07, 1.06824e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03242e+06, -878492 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 3.14e+09 s, dt: 4320000 s, Cycle: 797 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.09e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.09e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00724958 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605109 s | Solve Time: 0.174573 s + compositionalMultiphaseFlow: Max pressure change: 178.445 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33.534 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 1.01943840036256e-07 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.35e-04 ) + Last LinSolve(iter,res) = ( 2, 7.25e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99862e+06, 1.02727e+07, 1.06824e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03236e+06, -878567 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 3.15e+09 s, dt: 4320000 s, Cycle: 798 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.07e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 8.07e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00724908 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.602276 s | Solve Time: 0.174477 s + compositionalMultiphaseFlow: Max pressure change: 179.255 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 33.334 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 9.891777552617498e-08 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-04 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 1.35e-04 ) + Last LinSolve(iter,res) = ( 2, 7.25e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.99867e+06, 1.02727e+07, 1.06823e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03231e+06, -878642 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Time: 3.15e+09 s, dt: 2760000 s, Cycle: 799 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-03 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.16e-03 ) + MGR preconditioner: numComponentsPerField = [3, 4] + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00473182 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.605406 s | Solve Time: 0.174235 s + compositionalMultiphaseFlow: Max pressure change: 111.599 Pa (before scaling) + compositionalMultiphaseFlow: Max component density change: 21.225 mol/m3 (before scaling) + reservoirSystem: Global solution scaling factor = 1 +compositionalMultiphaseFlow: Max deltaPhaseVolFrac = 2.210267683322442e-06 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-05 ) ( Rwell ) = ( 0.00e+00 ) ( R ) = ( 5.53e-05 ) + Last LinSolve(iter,res) = ( 2, 4.73e-03 ) +wellControls1: well is shut +wellControls2: well is shut +compositionalMultiphaseFlow: Max relative pressure change during time step: 0.001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change during time step: 0.000 +reservoirSystem: Newton solver converged in less than 5 iterations, time-step required will be increased. +compflowStatistics, Region1: Pressure (min, average, max): 9.9987e+06, 1.02727e+07, 1.06822e+07 Pa +compflowStatistics, Region1: Delta pressure (min, max): -1.03225e+06, -878716 Pa +compflowStatistics, Region1: Temperature (min, average, max): 399.15, 399.15, 399.15 K +compflowStatistics, Region1: Total dynamic pore volume: 8e+08 rm^3 +compflowStatistics, Region1: Phase dynamic pore volumes: { 0, 8e+08 } rm^3 +compflowStatistics, Region1: Phase mass: { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Trapped phase mass (metric 1): { 0, 3.99817e+11 } mol +compflowStatistics, Region1: Non-trapped phase mass (metric 1): { 0, 2.26563e+12 } mol +compflowStatistics, Region1: Immobile phase mass (metric 2): { 0, 0 } mol +compflowStatistics, Region1: Mobile phase mass (metric 2): { 0, 2.66545e+12 } mol +compflowStatistics, Region1: Dissolved component mass: { { 0, 0 }, { 2.19553e+12, 4.69917e+11 } } mol +Cleaning up events +reservoirSystem, number of time steps: 803 +reservoirSystem, number of successful nonlinear iterations: 1132 +reservoirSystem, number of successful linear iterations: 4044 +reservoirSystem, number of time step cuts: 2 +reservoirSystem, number of discarded nonlinear iterations: 100 +reservoirSystem, number of discarded linear iterations: 3208 +reservoirSystem: apply solution time = 5.6296711 s (min), 5.6296711 s (max) +reservoirSystem: assemble time = 738.924959471 s (min), 738.924959471 s (max) +reservoirSystem: convergence check time = 4.709771653 s (min), 4.709771653 s (max) +reservoirSystem: linear solver create time = 233.226512227 s (min), 233.226512227 s (max) +reservoirSystem: linear solver setup time = 723.953565272 s (min), 723.953565272 s (max) +reservoirSystem: linear solver solve time = 709.917404124 s (min), 709.917404124 s (max) +reservoirSystem: linear solver total time = 1674.227316168 s (min), 1674.227316168 s (max) +reservoirSystem: update state time = 17024.703011053 s (min), 17024.703011053 s (max) +Umpire HOST sum across ranks: 529.6 MB +Umpire HOST rank max: 529.6 MB +Finished at 2024-01-31 16:43:29.848775440 +total time 07:44:30.613696435 +initialization time 00:00:12.394089953 +run time 07:44:11.038143480 diff --git a/geos-posp/tests/Data/empty.txt b/geos-posp/tests/Data/empty.txt new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/tests/Data/job_GEOS_246861.out b/geos-posp/tests/Data/job_GEOS_246861.out new file mode 100644 index 00000000..46c758c0 --- /dev/null +++ b/geos-posp/tests/Data/job_GEOS_246861.out @@ -0,0 +1,19729 @@ +GEOSX version: 0.2.0 (HEAD, sha1: c40be5d) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.26.0 +Adding Solver of type CompositionalMultiphaseReservoir, named compositionalMultiphaseReservoirSolver +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFVMSolver +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWellSolver +Adding Mesh: VTKMesh, mesh +Adding Mesh: InternalWell, wellInjector +Adding Event: PeriodicEvent, outputInjectionPeriod +Adding Event: PeriodicEvent, outputPostInjectionPeriod +Adding Event: PeriodicEvent, statistics +Adding Event: SoloEvent, soloStatistics +Adding Event: PeriodicEvent, solverApplicationInjectionPeriod +Adding Event: PeriodicEvent, solverApplicationPostInjectionPeriod1 +Adding Event: PeriodicEvent, solverApplicationPostInjectionPeriod2 +Adding Output: VTK, vtkOutput + TableFunction: initGasCompFracTable + TableFunction: initWaterCompFracTable + TableFunction: initTempTable + TableFunction: waterRelativePermeabilityTable + TableFunction: gasRelativePermeabilityTable + TableFunction: totalRateTable +Adding Object CellElementRegion named reservoir from ObjectManager::Catalog. +Adding Object CellElementRegion named reservoir_admunsen from ObjectManager::Catalog. +Adding Object WellElementRegion named well from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_EzrokhiBrineDensity_sat_density_table + TableFunction: fluid_phaseModel1_EzrokhiBrineDensity_sat_pressure_table + TableFunction: fluid_phaseModel1_EzrokhiBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table +VTK `vtkOutput`: found 8 fields to plot in `fieldNames`. These fields will be output regardless of the `plotLevel` specified by the user. No other field will be output. + TableFunction: wellControls_ConstantBHP_table + TableFunction: wellControls_ConstantPhaseRate_table +VTKMesh 'mesh': reading mesh from /work206/workrd/users/j0459652/GEOSX/nl_hexdom_margaux/04_hexdom_10m_with_uvw_with_properties_from_structured_grid_reservoir.vtu +Generating global Ids from VTK mesh +VTKMesh 'mesh': generating GEOSX mesh data structure +Number of nodes: 715020 + Number of elems: 475821 + C3D4: 705248 + C3D5: 221014 + C3D8: 475821 +Load balancing: min avg max +(element/rank): 421 4956 15051 + +++++++++++++++++++++++++++ +InternalWellGenerator = wellInjector +MPI rank = 0 + +Number of well elements = 16 +Well element #0 +Coordinates of the element center: { 524560, 6.71631e+06, -2606.5 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 524560, 6.71631e+06, -2618 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 524560, 6.71631e+06, -2628 } +Next well element # = 1 +Previous well element #3 +First well node: #2 +Second well node: #3 +Well element #3 +Coordinates of the element center: { 524560, 6.71631e+06, -2638 } +Next well element # = 2 +Previous well element #4 +First well node: #3 +Second well node: #4 +Well element #4 +Coordinates of the element center: { 524560, 6.71631e+06, -2648 } +Next well element # = 3 +Previous well element #5 +First well node: #4 +Second well node: #5 +Well element #5 +Coordinates of the element center: { 524560, 6.71631e+06, -2658 } +Next well element # = 4 +Previous well element #6 +First well node: #5 +Second well node: #6 +Well element #6 +Coordinates of the element center: { 524560, 6.71631e+06, -2668 } +Next well element # = 5 +Previous well element #7 +First well node: #6 +Second well node: #7 +Well element #7 +Coordinates of the element center: { 524560, 6.71631e+06, -2678 } +Next well element # = 6 +Previous well element #8 +First well node: #7 +Second well node: #8 +Well element #8 +Coordinates of the element center: { 524560, 6.71631e+06, -2688 } +Next well element # = 7 +Previous well element #9 +First well node: #8 +Second well node: #9 +Well element #9 +Coordinates of the element center: { 524560, 6.71631e+06, -2698 } +Next well element # = 8 +Previous well element #10 +First well node: #9 +Second well node: #10 +Well element #10 +Coordinates of the element center: { 524560, 6.71631e+06, -2708 } +Next well element # = 9 +Previous well element #11 +First well node: #10 +Second well node: #11 +Well element #11 +Coordinates of the element center: { 524560, 6.71631e+06, -2718 } +Next well element # = 10 +Previous well element #12 +First well node: #11 +Second well node: #12 +Well element #12 +Coordinates of the element center: { 524560, 6.71631e+06, -2728 } +Next well element # = 11 +Previous well element #13 +First well node: #12 +Second well node: #13 +Well element #13 +Coordinates of the element center: { 524560, 6.71631e+06, -2738 } +Next well element # = 12 +Previous well element #14 +First well node: #13 +Second well node: #14 +Well element #14 +Coordinates of the element center: { 524560, 6.71631e+06, -2748 } +Next well element # = 13 +Previous well element #15 +First well node: #14 +Second well node: #15 +Well element #15 +Coordinates of the element center: { 524560, 6.71631e+06, -2758 } +Next well element # = 14 +No previous well element +First well node: #15 +Second well node: #16 + +Number of perforations = 16 +Perforation #0 +Coordinates of the perforation: { 524560, 6.71631e+06, -2610.5 } +Is connected to well element #0 +Perforation #1 +Coordinates of the perforation: { 524560, 6.71631e+06, -2619.5 } +Is connected to well element #1 +Perforation #2 +Coordinates of the perforation: { 524560, 6.71631e+06, -2628.5 } +Is connected to well element #2 +Perforation #3 +Coordinates of the perforation: { 524560, 6.71631e+06, -2637.9 } +Is connected to well element #3 +Perforation #4 +Coordinates of the perforation: { 524560, 6.71631e+06, -2647 } +Is connected to well element #4 +Perforation #5 +Coordinates of the perforation: { 524560, 6.71631e+06, -2656.5 } +Is connected to well element #5 +Perforation #6 +Coordinates of the perforation: { 524560, 6.71631e+06, -2666.5 } +Is connected to well element #6 +Perforation #7 +Coordinates of the perforation: { 524560, 6.71631e+06, -2676.5 } +Is connected to well element #7 +Perforation #8 +Coordinates of the perforation: { 524560, 6.71631e+06, -2686.5 } +Is connected to well element #8 +Perforation #9 +Coordinates of the perforation: { 524560, 6.71631e+06, -2696.5 } +Is connected to well element #9 +Perforation #10 +Coordinates of the perforation: { 524560, 6.71631e+06, -2706.5 } +Is connected to well element #10 +Perforation #11 +Coordinates of the perforation: { 524560, 6.71631e+06, -2716.5 } +Is connected to well element #11 +Perforation #12 +Coordinates of the perforation: { 524560, 6.71631e+06, -2726.3 } +Is connected to well element #12 +Perforation #13 +Coordinates of the perforation: { 524560, 6.71631e+06, -2736.3 } +Is connected to well element #13 +Perforation #14 +Coordinates of the perforation: { 524560, 6.71631e+06, -2746.3 } +Is connected to well element #14 +Perforation #15 +Coordinates of the perforation: { 524560, 6.71631e+06, -2756.3 } +Is connected to well element #15 + +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_hexahedra +mesh/Level0/reservoir/2_hexahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_pyramids +mesh/Level0/reservoir/2_pyramids/rock allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_tetrahedra +mesh/Level0/reservoir/2_tetrahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_hexahedra +mesh/Level0/reservoir/3_hexahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_pyramids +mesh/Level0/reservoir/3_pyramids/rock allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_tetrahedra +mesh/Level0/reservoir/3_tetrahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, well, wellUniqueSubRegion +mesh/Level0/well/wellUniqueSubRegion/fluid allocated 1 quadrature points +mesh/Level0/well/wellUniqueSubRegion/relperm allocated 1 quadrature points + TableFunction: equil_2_hexahedra_water_table + TableFunction: equil_2_tetrahedra_water_table + TableFunction: equil_2_pyramids_water_table + TableFunction: equil_3_hexahedra_water_table + TableFunction: equil_3_tetrahedra_water_table + TableFunction: equil_3_pyramids_water_table +Time: 0s, dt:8600s, Cycle: 0 +compflowStatistics, reservoir: Pressure (min, average, max): 2.0159e+07, 2.68032e+07, 3.89368e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45705e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0, 3.45705e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 0, 3.35481e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00644e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 0, 0 }, { 0, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.12e+02 ) ; ( R ) = ( 3.12e+02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 5.96636e-05 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 1.5156 s | Solve Time: 0.041093 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 3.49e-04 ) ; ( R ) = ( 6.01e-04 ) ; + Last LinSolve(iter,res) = ( 1, 5.97e-05 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0884298 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 6.29211e-09 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8600s, dt:17124.3s, Cycle: 1 +wellControls: BHP (at the specified reference elevation): 27452073.075918034 Pa +wellControls: Total rate: 49.49343235863489 kg/s; total surface volumetric rate: 26.524664060614963 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52466406061294 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0274305932361715e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 3.60e-04 ) ; ( R ) = ( 4.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00144374 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.327855 s | Solve Time: 0.0461692 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 4.13e-06 ) ; ( R ) = ( 3.10e-05 ) ; + Last LinSolve(iter,res) = ( 2, 1.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0487591 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 2.10852e-08 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 25724.3s, dt:34165.3s, Cycle: 2 +wellControls: BHP (at the specified reference elevation): 27375394.375235207 Pa +wellControls: Total rate: 49.485508293503074 kg/s; total surface volumetric rate: 26.5204173726081 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.520417372606076 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059947731947e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.13e-03 ) ; ( Rwell ) = ( 4.14e-06 ) ; ( R ) = ( 8.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0019764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.336642 s | Solve Time: 0.0473239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-04 ) ; ( Rwell ) = ( 6.43e-06 ) ; ( R ) = ( 1.33e-04 ) ; + Last LinSolve(iter,res) = ( 2, 1.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0263923 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 8.11139e-08 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 59889.6s, dt:68240.5s, Cycle: 3 +wellControls: BHP (at the specified reference elevation): 27379150.169630803 Pa +wellControls: Total rate: 49.485507598095694 kg/s; total surface volumetric rate: 26.52041699992336 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699992133 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.027105966286785e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 6.43e-06 ) ; ( R ) = ( 1.62e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0023484 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.288896 s | Solve Time: 0.045903 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 5.82e-06 ) ; ( R ) = ( 3.71e-04 ) ; + Last LinSolve(iter,res) = ( 2, 2.35e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0234117 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 3.19704e-07 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 128130s, dt:136321s, Cycle: 4 +wellControls: BHP (at the specified reference elevation): 27382328.766091175 Pa +wellControls: Total rate: 49.485507598238726 kg/s; total surface volumetric rate: 26.520417000000013 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.520416999997988 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.027105966292644e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 5.82e-06 ) ; ( R ) = ( 3.23e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00911411 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.347605 s | Solve Time: 0.0262511 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.61e-05 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 1, 9.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0250243 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 1.22826e-06 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 264451s, dt:272302s, Cycle: 5 +wellControls: BHP (at the specified reference elevation): 27384640.62430385 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 4.61e-05 ) ; ( R ) = ( 6.40e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0028687 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.314962 s | Solve Time: 0.0498346 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.35e-06 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 2, 2.87e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0251283 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 4.71821e-06 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 536754s, dt:543921s, Cycle: 6 +wellControls: BHP (at the specified reference elevation): 27387666.304275896 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 6.35e-06 ) ; ( R ) = ( 1.27e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00974227 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.271858 s | Solve Time: 0.027884 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.35e-04 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 1, 9.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00814889 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.245199 s | Solve Time: 0.11066 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 5.83e-05 ) ; ( R ) = ( 5.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.300486 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0376635 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.08067e+06s, dt:869515s, Cycle: 7 +wellControls: BHP (at the specified reference elevation): 27488532.372734226 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 5.83e-05 ) ; ( R ) = ( 1.75e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0063298 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234164 s | Solve Time: 0.110448 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 3.02e-04 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00584461 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.232428 s | Solve Time: 0.129718 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.46e-03 ) ; ( Rwell ) = ( 3.07e-04 ) ; ( R ) = ( 9.46e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.765113 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0736742 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.95019e+06s, dt:1.16623e+06s, Cycle: 8 +wellControls: BHP (at the specified reference elevation): 27907245.229570244 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 3.07e-04 ) ; ( R ) = ( 2.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00533133 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.244703 s | Solve Time: 0.108793 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 1.31e-04 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0042907 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.269929 s | Solve Time: 0.130566 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 5.29e-05 ) ; ( R ) = ( 5.84e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.899452 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0765442 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.11642e+06s, dt:1.54437e+06s, Cycle: 9 +wellControls: BHP (at the specified reference elevation): 28338830.559048314 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.31e-01 ) ; ( Rwell ) = ( 5.28e-05 ) ; ( R ) = ( 2.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00455441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.27084 s | Solve Time: 0.0897772 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 5.36e-04 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00447927 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208565 s | Solve Time: 0.0892904 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.44e-05 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.494726 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0698899 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.66078e+06s, dt:2.10701e+06s, Cycle: 10 +wellControls: BHP (at the specified reference elevation): 28515925.8330221 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 1.44e-05 ) ; ( R ) = ( 2.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00812344 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.243836 s | Solve Time: 0.0883089 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 1.59e-04 ) ; ( R ) = ( 1.16e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00759132 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220505 s | Solve Time: 0.130936 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 1.17e-05 ) ; ( R ) = ( 4.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00611048 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.232972 s | Solve Time: 0.067764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.19e-07 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.118533 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0814816 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.76779e+06s, dt:2.73068e+06s, Cycle: 11 +wellControls: BHP (at the specified reference elevation): 28468780.07603685 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 3.20e-07 ) ; ( R ) = ( 2.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00942445 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213317 s | Solve Time: 0.0702973 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 2.58e-05 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00364473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22473 s | Solve Time: 0.151583 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 7.23e-06 ) ; ( R ) = ( 1.08e-01 ) ; + Last LinSolve(iter,res) = ( 7, 3.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00336146 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206807 s | Solve Time: 0.0681426 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 1.73e-06 ) ; ( R ) = ( 6.81e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.36e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.338648 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0947419 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.49848e+06s, dt:3.34722e+06s, Cycle: 12 +wellControls: BHP (at the specified reference elevation): 28391007.85920798 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 1.73e-06 ) ; ( R ) = ( 3.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00877512 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208317 s | Solve Time: 0.0907566 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 1.12e-05 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00949237 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21683 s | Solve Time: 0.0889164 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.13e-02 ) ; ( Rwell ) = ( 2.92e-06 ) ; ( R ) = ( 7.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00550383 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222059 s | Solve Time: 0.0892109 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 3.35e-07 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.286869 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.117847 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.28457e+07s, dt:3.74903e+06s, Cycle: 13 +wellControls: BHP (at the specified reference elevation): 28303043.972354457 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-01 ) ; ( Rwell ) = ( 3.35e-07 ) ; ( R ) = ( 3.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00779558 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206537 s | Solve Time: 0.132757 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 1.38e-05 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00477387 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.233098 s | Solve Time: 0.145102 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.12e-06 ) ; ( R ) = ( 4.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00715308 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217987 s | Solve Time: 0.0471347 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 2, 7.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.101563 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.078322 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.65947e+07s, dt:4.92598e+06s, Cycle: 14 +wellControls: BHP (at the specified reference elevation): 28203593.64870266 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-01 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 3.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00742916 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222033 s | Solve Time: 0.129357 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 9.27e-06 ) ; ( R ) = ( 2.42e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00881956 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210866 s | Solve Time: 0.129561 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 8.78e-06 ) ; ( R ) = ( 8.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00882942 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209606 s | Solve Time: 0.0686991 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 3.75e-07 ) ; ( R ) = ( 5.54e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.178122 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133278 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.15207e+07s, dt:5.21677e+06s, Cycle: 15 +wellControls: BHP (at the specified reference elevation): 28130358.53383725 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 3.76e-07 ) ; ( R ) = ( 3.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00843707 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208427 s | Solve Time: 0.0885632 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 7.86e-06 ) ; ( R ) = ( 2.87e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00839973 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228706 s | Solve Time: 0.109114 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 5.29e-06 ) ; ( R ) = ( 1.91e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00695554 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207892 s | Solve Time: 0.068572 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00528752 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211649 s | Solve Time: 0.108929 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.56e-04 ) ; ( Rwell ) = ( 3.03e-08 ) ; ( R ) = ( 3.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.348024 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.11901 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.67375e+07s, dt:5.81773e+06s, Cycle: 16 +wellControls: BHP (at the specified reference elevation): 28102583.934757862 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-01 ) ; ( Rwell ) = ( 3.03e-08 ) ; ( R ) = ( 4.23e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00683979 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209334 s | Solve Time: 0.116986 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 4.00e-06 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00690052 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210676 s | Solve Time: 0.0887524 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 4.25e-06 ) ; ( R ) = ( 7.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00778475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207119 s | Solve Time: 0.0683923 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 8.11e-07 ) ; ( R ) = ( 6.79e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.240602 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0965669 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.25552e+07s, dt:7.07848e+06s, Cycle: 17 +wellControls: BHP (at the specified reference elevation): 28067434.75114054 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-01 ) ; ( Rwell ) = ( 8.11e-07 ) ; ( R ) = ( 4.79e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00767649 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226769 s | Solve Time: 0.132078 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 6.25e-06 ) ; ( R ) = ( 3.57e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00424535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21068 s | Solve Time: 0.131833 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 5.46e-06 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0070666 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222392 s | Solve Time: 0.0683077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 4.38e-07 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0072555 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214462 s | Solve Time: 0.110152 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 2.82e-08 ) ; ( R ) = ( 5.26e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.194477 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.109561 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.96337e+07s, dt:8.18129e+06s, Cycle: 18 +wellControls: BHP (at the specified reference elevation): 28036616.070012707 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-01 ) ; ( Rwell ) = ( 2.82e-08 ) ; ( R ) = ( 5.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00862258 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226852 s | Solve Time: 0.110286 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-01 ) ; ( Rwell ) = ( 7.32e-06 ) ; ( R ) = ( 4.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00478003 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213382 s | Solve Time: 0.130592 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 4.67e-06 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00728957 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208581 s | Solve Time: 0.0699517 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.14e-03 ) ; ( Rwell ) = ( 2.78e-07 ) ; ( R ) = ( 9.14e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.320437 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.13548 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.7815e+07s, dt:8.59741e+06s, Cycle: 19 +wellControls: BHP (at the specified reference elevation): 28023026.232618887 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-01 ) ; ( Rwell ) = ( 2.78e-07 ) ; ( R ) = ( 5.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00570712 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216154 s | Solve Time: 0.129355 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.92e-01 ) ; ( Rwell ) = ( 6.24e-06 ) ; ( R ) = ( 9.92e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-01 ) ; ( Rwell ) = ( 2.67e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00539257 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205156 s | Solve Time: 0.130611 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 2.94e-06 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00817003 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211665 s | Solve Time: 0.0912041 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00708629 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227245 s | Solve Time: 0.0899748 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.247091 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.130578 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.64124e+07s, dt:9.19255e+06s, Cycle: 20 +wellControls: BHP (at the specified reference elevation): 28016770.35888808 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-01 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 5.27e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00708628 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215082 s | Solve Time: 0.109446 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e+00 ) ; ( Rwell ) = ( 9.34e-06 ) ; ( R ) = ( 1.12e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-01 ) ; ( Rwell ) = ( 4.51e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00671829 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218305 s | Solve Time: 0.109353 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 4.05e-06 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00826256 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22417 s | Solve Time: 0.067989 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00625176 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207482 s | Solve Time: 0.10889 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.22e-04 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 3.22e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.25e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.254566 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.113746 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.56049e+07s, dt:1.04561e+07s, Cycle: 21 +wellControls: BHP (at the specified reference elevation): 28013746.409194853 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-01 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 5.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00768316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225223 s | Solve Time: 0.131595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.16e-01 ) ; ( Rwell ) = ( 8.72e-06 ) ; ( R ) = ( 6.16e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 4.31e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00917324 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222965 s | Solve Time: 0.131816 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 1.13e-05 ) ; ( R ) = ( 2.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00707054 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221774 s | Solve Time: 0.0886263 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 3.54e-07 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00584154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208583 s | Solve Time: 0.1117 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.13e-04 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 3.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.414909 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.108567 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.60611e+07s, dt:1.21316e+07s, Cycle: 22 +wellControls: BHP (at the specified reference elevation): 28019476.750873815 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.18e-01 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 6.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00703949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217611 s | Solve Time: 0.111414 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.98e-01 ) ; ( Rwell ) = ( 1.26e-05 ) ; ( R ) = ( 7.98e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 6.27e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00689429 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208503 s | Solve Time: 0.131051 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.33e-01 ) ; ( Rwell ) = ( 8.40e-06 ) ; ( R ) = ( 3.33e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00590802 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207226 s | Solve Time: 0.109402 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 3.09e-06 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0092085 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229201 s | Solve Time: 0.0892201 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.66e-03 ) ; ( Rwell ) = ( 7.74e-08 ) ; ( R ) = ( 7.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.310013 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.130243 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.81927e+07s, dt:1.29869e+07s, Cycle: 23 +wellControls: BHP (at the specified reference elevation): 28033196.364663474 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.39e-01 ) ; ( Rwell ) = ( 7.74e-08 ) ; ( R ) = ( 6.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00702353 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229086 s | Solve Time: 0.11125 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.25e-01 ) ; ( Rwell ) = ( 1.41e-05 ) ; ( R ) = ( 8.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 6.94e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00647755 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230223 s | Solve Time: 0.133063 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 9.86e-06 ) ; ( R ) = ( 2.35e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844776 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205466 s | Solve Time: 0.112086 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 3.44e-06 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00629756 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211042 s | Solve Time: 0.11005 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.30e-03 ) ; +wellControls: BHP (at the specified reference elevation): 28053114.170068875 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.282741 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.134628 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.0118e+08s, dt:1.36883e+07s, Cycle: 24 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.43e-01 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 6.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00847431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210115 s | Solve Time: 0.110246 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 1.10e-05 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 5.40e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00724992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226299 s | Solve Time: 0.129366 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 7.66e-06 ) ; ( R ) = ( 3.45e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00852471 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206018 s | Solve Time: 0.0883156 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.73e-06 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00390265 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.23143 s | Solve Time: 0.108769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.86e-08 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.272157 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.109738 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.14868e+08s, dt:1.58101e+07s, Cycle: 25 +wellControls: BHP (at the specified reference elevation): 28076795.712509252 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.95e-01 ) ; ( Rwell ) = ( 7.86e-08 ) ; ( R ) = ( 6.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00988696 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208433 s | Solve Time: 0.110903 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.85e-01 ) ; ( Rwell ) = ( 2.20e-05 ) ; ( R ) = ( 6.85e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00863208 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206952 s | Solve Time: 0.109312 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 1.14e-05 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00858726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209499 s | Solve Time: 0.0907276 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0067406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221795 s | Solve Time: 0.111138 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 7.18e-08 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.279061 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.118886 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.30678e+08s, dt:1.76395e+07s, Cycle: 26 +wellControls: BHP (at the specified reference elevation): 28104230.64885674 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.44e-01 ) ; ( Rwell ) = ( 7.18e-08 ) ; ( R ) = ( 7.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00632672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207144 s | Solve Time: 0.132195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e+00 ) ; ( Rwell ) = ( 8.85e-06 ) ; ( R ) = ( 1.89e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.00e-01 ) ; ( Rwell ) = ( 4.35e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0098292 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.235114 s | Solve Time: 0.130097 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-01 ) ; ( Rwell ) = ( 8.10e-06 ) ; ( R ) = ( 6.56e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-01 ) ; ( Rwell ) = ( 6.21e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00556794 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224734 s | Solve Time: 0.154258 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 2.32e-06 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00992045 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21552 s | Solve Time: 0.0692244 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00641725 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211182 s | Solve Time: 0.112756 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.65e-04 ) ; ( Rwell ) = ( 2.32e-08 ) ; ( R ) = ( 3.65e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.302835 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.137641 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.48317e+08s, dt:9.36253e+06s, Cycle: 27 +wellControls: BHP (at the specified reference elevation): 28145794.856397364 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 2.32e-08 ) ; ( R ) = ( 3.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00743553 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234294 s | Solve Time: 0.112527 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 8.43e-06 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00690248 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.231476 s | Solve Time: 0.111589 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00935368 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213046 s | Solve Time: 0.0921705 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.80e-07 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; +wellControls: BHP (at the specified reference elevation): 28171935.456630044 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.177799 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0752042 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.5768e+08s, dt:1.24721e+07s, Cycle: 28 +compflowStatistics, reservoir: Pressure (min, average, max): 2.05853e+07, 2.73111e+07, 3.91351e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 160793, 962034 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45722e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 9.16636e+06, 3.45631e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 5.71764e+09, 3.35489e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00674e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 5.71764e+09, 0 }, { 2.08527e+09, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-01 ) ; ( Rwell ) = ( 1.80e-07 ) ; ( R ) = ( 5.03e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00600949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217491 s | Solve Time: 0.131008 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.66e-01 ) ; ( Rwell ) = ( 1.91e-06 ) ; ( R ) = ( 5.66e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00622505 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230796 s | Solve Time: 0.131053 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 1.51e-06 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00703497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220317 s | Solve Time: 0.069404 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 5.59e-07 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00429178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206189 s | Solve Time: 0.109718 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 5.28e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.20978 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.1057 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.70152e+08s, dt:1.46328e+07s, Cycle: 29 +wellControls: BHP (at the specified reference elevation): 28199619.857583474 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-01 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 5.75e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00992949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206122 s | Solve Time: 0.109041 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.52e-01 ) ; ( Rwell ) = ( 5.85e-06 ) ; ( R ) = ( 6.52e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 2.91e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00981745 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216627 s | Solve Time: 0.132915 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 2.11e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00491506 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213856 s | Solve Time: 0.0939403 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.27e-06 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00740297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.231883 s | Solve Time: 0.0938596 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 9.15e-08 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.250185 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.129899 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.84785e+08s, dt:1.56837e+07s, Cycle: 30 +wellControls: BHP (at the specified reference elevation): 28233952.05256419 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-01 ) ; ( Rwell ) = ( 9.15e-08 ) ; ( R ) = ( 5.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00487578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217038 s | Solve Time: 0.129772 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.38e-01 ) ; ( Rwell ) = ( 1.54e-06 ) ; ( R ) = ( 7.38e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-01 ) ; ( Rwell ) = ( 7.73e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00524136 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206598 s | Solve Time: 0.157201 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 1.73e-06 ) ; ( R ) = ( 2.60e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.008197 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225864 s | Solve Time: 0.089768 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.95e-06 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00714801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217445 s | Solve Time: 0.0907476 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.55e-07 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.259851 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12402 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.00469e+08s, dt:1.71707e+07s, Cycle: 31 +wellControls: BHP (at the specified reference elevation): 28274501.286368474 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-01 ) ; ( Rwell ) = ( 1.55e-07 ) ; ( R ) = ( 6.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00612185 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211459 s | Solve Time: 0.130429 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e+00 ) ; ( Rwell ) = ( 3.36e-06 ) ; ( R ) = ( 4.23e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e+00 ) ; ( Rwell ) = ( 1.61e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-01 ) ; ( Rwell ) = ( 7.30e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.29e-01 ) ; ( Rwell ) = ( 2.91e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00598189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209278 s | Solve Time: 0.199653 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e+00 ) ; ( Rwell ) = ( 1.29e-06 ) ; ( R ) = ( 2.19e+00 ) ; + Last LinSolve(iter,res) = ( 9, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.94e-01 ) ; ( Rwell ) = ( 6.95e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-01 ) ; ( Rwell ) = ( 4.54e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00581947 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219516 s | Solve Time: 0.173484 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e+00 ) ; ( Rwell ) = ( 2.11e-06 ) ; ( R ) = ( 1.12e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-01 ) ; ( Rwell ) = ( 8.48e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00576557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225815 s | Solve Time: 0.130021 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 2.00e-06 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00895085 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210817 s | Solve Time: 0.0709573 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00845935 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206968 s | Solve Time: 0.109297 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.43e-04 ) ; ( Rwell ) = ( 5.03e-08 ) ; ( R ) = ( 4.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.283376 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.156302 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.17639e+08s, dt:1.68174e+07s, Cycle: 32 +wellControls: BHP (at the specified reference elevation): 28319890.904760633 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.18e-01 ) ; ( Rwell ) = ( 5.03e-08 ) ; ( R ) = ( 6.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00745279 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214018 s | Solve Time: 0.130616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e+00 ) ; ( Rwell ) = ( 3.68e-06 ) ; ( R ) = ( 1.33e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-01 ) ; ( Rwell ) = ( 1.81e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00495061 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216164 s | Solve Time: 0.15134 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.30e-01 ) ; ( Rwell ) = ( 8.82e-07 ) ; ( R ) = ( 6.30e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 5.93e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.009598 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205075 s | Solve Time: 0.129813 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 1.82e-06 ) ; ( R ) = ( 1.51e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0083873 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205593 s | Solve Time: 0.108614 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 6.39e-07 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00367825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205761 s | Solve Time: 0.131177 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-04 ) ; ( Rwell ) = ( 2.51e-08 ) ; ( R ) = ( 1.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 3.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.276953 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.121733 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.34457e+08s, dt:1.85669e+07s, Cycle: 33 +wellControls: BHP (at the specified reference elevation): 28365760.204258803 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-01 ) ; ( Rwell ) = ( 2.51e-08 ) ; ( R ) = ( 6.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00903724 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212223 s | Solve Time: 0.13057 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e+00 ) ; ( Rwell ) = ( 2.88e-06 ) ; ( R ) = ( 1.86e+00 ) ; + Last LinSolve(iter,res) = ( 6, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.37e-01 ) ; ( Rwell ) = ( 1.41e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-01 ) ; ( Rwell ) = ( 6.93e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00955193 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206281 s | Solve Time: 0.152899 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.37e-01 ) ; ( Rwell ) = ( 5.15e-06 ) ; ( R ) = ( 5.37e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 2.91e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00741969 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205867 s | Solve Time: 0.15146 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.05e-01 ) ; ( Rwell ) = ( 3.42e-07 ) ; ( R ) = ( 3.05e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00372622 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.232039 s | Solve Time: 0.0981608 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.02e-06 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00807075 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226871 s | Solve Time: 0.0883188 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 1.97e-08 ) ; ( R ) = ( 9.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.305617 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.15723 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.53024e+08s, dt:1.81299e+07s, Cycle: 34 +wellControls: BHP (at the specified reference elevation): 28417727.670362625 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.54e-01 ) ; ( Rwell ) = ( 1.97e-08 ) ; ( R ) = ( 6.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00469594 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214166 s | Solve Time: 0.154558 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e+00 ) ; ( Rwell ) = ( 4.85e-07 ) ; ( R ) = ( 2.08e+00 ) ; + Last LinSolve(iter,res) = ( 7, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.16e-01 ) ; ( Rwell ) = ( 2.12e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00699438 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214377 s | Solve Time: 0.131317 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-01 ) ; ( Rwell ) = ( 2.94e-06 ) ; ( R ) = ( 3.50e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00930587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213405 s | Solve Time: 0.108464 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00390283 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210519 s | Solve Time: 0.108404 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.296449 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.129554 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.71154e+08s, dt:1.94559e+07s, Cycle: 35 +wellControls: BHP (at the specified reference elevation): 28467660.285742506 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.16e-01 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 7.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00507714 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212111 s | Solve Time: 0.150898 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e+00 ) ; ( Rwell ) = ( 8.72e-07 ) ; ( R ) = ( 1.27e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 4.75e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00756542 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208935 s | Solve Time: 0.150982 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.72e-01 ) ; ( Rwell ) = ( 5.33e-07 ) ; ( R ) = ( 7.72e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-01 ) ; ( Rwell ) = ( 4.78e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00757217 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206759 s | Solve Time: 0.153252 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 7.32e-07 ) ; ( R ) = ( 2.56e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00510925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209237 s | Solve Time: 0.114162 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 3.73e-07 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0063164 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214576 s | Solve Time: 0.153665 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 6.85e-09 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.32e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.3183 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145571 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.90609e+08s, dt:1.97475e+07s, Cycle: 36 +wellControls: BHP (at the specified reference elevation): 28525035.763980683 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.99e-01 ) ; ( Rwell ) = ( 6.85e-09 ) ; ( R ) = ( 7.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00535855 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205526 s | Solve Time: 0.170993 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e+00 ) ; ( Rwell ) = ( 4.53e-07 ) ; ( R ) = ( 4.13e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e+00 ) ; ( Rwell ) = ( 1.78e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.78e-01 ) ; ( Rwell ) = ( 7.40e-08 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00857979 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208021 s | Solve Time: 0.152115 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.07e+00 ) ; ( Rwell ) = ( 2.15e-06 ) ; ( R ) = ( 4.07e+00 ) ; + Last LinSolve(iter,res) = ( 7, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e+00 ) ; ( Rwell ) = ( 1.06e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.90e-01 ) ; ( Rwell ) = ( 5.21e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-01 ) ; ( Rwell ) = ( 2.55e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00809466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216363 s | Solve Time: 0.173966 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e+00 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 1.45e+00 ) ; + Last LinSolve(iter,res) = ( 8, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-01 ) ; ( Rwell ) = ( 6.51e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0076325 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205797 s | Solve Time: 0.200454 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.59e-01 ) ; ( Rwell ) = ( 5.24e-07 ) ; ( R ) = ( 9.59e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-01 ) ; ( Rwell ) = ( 5.65e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00779271 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224536 s | Solve Time: 0.173999 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.19e-01 ) ; ( Rwell ) = ( 2.07e-07 ) ; ( R ) = ( 4.19e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00602473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225689 s | Solve Time: 0.0904365 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.05e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 7.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00892749 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222716 s | Solve Time: 0.13411 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 7.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.32484 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.201807 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.10357e+08s, dt:5.003e+06s, Cycle: 37 +wellControls: BHP (at the specified reference elevation): 28582978.51677252 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 2.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00685265 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221183 s | Solve Time: 0.110183 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 2.09e-06 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00616955 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208776 s | Solve Time: 0.131712 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 5.54e-08 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.17e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.106764 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0727031 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.1536e+08s, dt:6.73947e+06s, Cycle: 38 +wellControls: BHP (at the specified reference elevation): 28600264.361991383 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.11243e+07, 2.7845e+07, 3.95579e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 578747, 1.4774e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45741e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.89444e+07, 3.45551e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 1.19678e+10, 3.35495e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00704e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1.19678e+10, 0 }, { 3.63798e+09, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 5.54e-08 ) ; ( R ) = ( 3.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00557673 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227758 s | Solve Time: 0.155489 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.18e-01 ) ; ( Rwell ) = ( 3.17e-07 ) ; ( R ) = ( 6.18e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-01 ) ; ( Rwell ) = ( 1.62e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0040143 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211438 s | Solve Time: 0.140337 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.56e-01 ) ; ( Rwell ) = ( 6.58e-07 ) ; ( R ) = ( 7.56e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 3.63e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00598619 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218981 s | Solve Time: 0.152175 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.93e-01 ) ; ( Rwell ) = ( 1.91e-07 ) ; ( R ) = ( 8.93e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 1.06e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 2.31e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00772747 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225736 s | Solve Time: 0.137828 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.51e-01 ) ; ( Rwell ) = ( 4.94e-07 ) ; ( R ) = ( 9.51e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-01 ) ; ( Rwell ) = ( 1.48e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 7.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 1.47e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00826084 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212516 s | Solve Time: 0.131075 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.55e-02 ) ; ( Rwell ) = ( 3.96e-07 ) ; ( R ) = ( 7.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00590045 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207829 s | Solve Time: 0.132144 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00765289 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223617 s | Solve Time: 0.109485 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.112939 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.166388 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.22099e+08s, dt:6.39039e+06s, Cycle: 39 +wellControls: BHP (at the specified reference elevation): 28620166.33878346 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.81e-01 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 3.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00822768 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207061 s | Solve Time: 0.131642 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.10e-01 ) ; ( Rwell ) = ( 2.13e-06 ) ; ( R ) = ( 6.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-01 ) ; ( Rwell ) = ( 1.06e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00606419 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208198 s | Solve Time: 0.192516 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.49e-01 ) ; ( Rwell ) = ( 1.78e-07 ) ; ( R ) = ( 7.49e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 5.28e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00640946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211566 s | Solve Time: 0.150389 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 8.84e-08 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 7, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 2.92e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00695988 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220538 s | Solve Time: 0.158055 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.14e-07 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00482476 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214367 s | Solve Time: 0.172967 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.26e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 2.26e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.82e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.112303 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.129605 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.2849e+08s, dt:6.85652e+06s, Cycle: 40 +wellControls: BHP (at the specified reference elevation): 28638903.55416524 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-01 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 4.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0062545 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225034 s | Solve Time: 0.178714 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e+00 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 2.15e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.03e-01 ) ; ( Rwell ) = ( 5.34e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-01 ) ; ( Rwell ) = ( 2.65e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00337002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22213 s | Solve Time: 0.21582 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e+00 ) ; ( Rwell ) = ( 1.97e-07 ) ; ( R ) = ( 1.68e+00 ) ; + Last LinSolve(iter,res) = ( 10, 3.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.42e-01 ) ; ( Rwell ) = ( 2.27e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-01 ) ; ( Rwell ) = ( 2.46e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 2.55e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00805955 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221381 s | Solve Time: 0.175144 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.13e-01 ) ; ( Rwell ) = ( 4.59e-07 ) ; ( R ) = ( 6.13e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 3.47e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00720307 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227175 s | Solve Time: 0.178359 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-01 ) ; ( Rwell ) = ( 3.68e-07 ) ; ( R ) = ( 3.02e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00584812 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228201 s | Solve Time: 0.151265 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00862788 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2242 s | Solve Time: 0.130412 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.40e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; ( R ) = ( 1.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.117675 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.249781 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.35346e+08s, dt:5.14521e+06s, Cycle: 41 +wellControls: BHP (at the specified reference elevation): 28659771.760701213 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-01 ) ; ( Rwell ) = ( 3.84e-09 ) ; ( R ) = ( 3.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00467901 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220482 s | Solve Time: 0.157515 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e+00 ) ; ( Rwell ) = ( 2.11e-06 ) ; ( R ) = ( 1.07e+00 ) ; + Last LinSolve(iter,res) = ( 7, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 1.06e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00585455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213386 s | Solve Time: 0.175236 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e+00 ) ; ( Rwell ) = ( 5.26e-07 ) ; ( R ) = ( 2.04e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.22e-01 ) ; ( Rwell ) = ( 3.03e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-01 ) ; ( Rwell ) = ( 6.73e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 8.64e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0097387 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219927 s | Solve Time: 0.172561 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.91e+00 ) ; ( Rwell ) = ( 4.93e-07 ) ; ( R ) = ( 1.91e+00 ) ; + Last LinSolve(iter,res) = ( 8, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-01 ) ; ( Rwell ) = ( 6.75e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 7.69e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-01 ) ; ( Rwell ) = ( 8.16e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 8.40e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00836589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214612 s | Solve Time: 0.172696 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00941099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217739 s | Solve Time: 0.13115 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.31e-03 ) ; ( Rwell ) = ( 1.87e-07 ) ; ( R ) = ( 9.31e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.106614 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.135618 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.40492e+08s, dt:5.40429e+06s, Cycle: 42 +wellControls: BHP (at the specified reference elevation): 28675564.68220155 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 1.87e-07 ) ; ( R ) = ( 3.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00393334 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221016 s | Solve Time: 0.191271 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e+00 ) ; ( Rwell ) = ( 1.77e-06 ) ; ( R ) = ( 1.56e+00 ) ; + Last LinSolve(iter,res) = ( 9, 3.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 8.07e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.009922 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205654 s | Solve Time: 0.129983 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e+00 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 2.06e+00 ) ; + Last LinSolve(iter,res) = ( 6, 9.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 1.08e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 9.41e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00740925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213141 s | Solve Time: 0.134798 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e+00 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 2.21e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.02e-01 ) ; ( Rwell ) = ( 5.17e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 7.27e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00820317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210983 s | Solve Time: 0.213576 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 4.70e-07 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00837738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205658 s | Solve Time: 0.192907 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.32e-08 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0956669 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.134427 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.45896e+08s, dt:5.70018e+06s, Cycle: 43 +wellControls: BHP (at the specified reference elevation): 28691622.388488792 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-01 ) ; ( Rwell ) = ( 1.32e-08 ) ; ( R ) = ( 3.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00742792 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217525 s | Solve Time: 0.170765 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e+00 ) ; ( Rwell ) = ( 6.87e-07 ) ; ( R ) = ( 5.29e+00 ) ; + Last LinSolve(iter,res) = ( 8, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 3.38e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00603788 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209412 s | Solve Time: 0.195179 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.72e+00 ) ; ( Rwell ) = ( 7.32e-07 ) ; ( R ) = ( 4.72e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e+00 ) ; ( Rwell ) = ( 5.25e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 4.27e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00543251 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207739 s | Solve Time: 0.22634 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.06e+00 ) ; ( Rwell ) = ( 5.21e-07 ) ; ( R ) = ( 5.06e+00 ) ; + Last LinSolve(iter,res) = ( 10, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e+00 ) ; ( Rwell ) = ( 4.69e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 4.47e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-01 ) ; ( Rwell ) = ( 4.36e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 4.32e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00857915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224549 s | Solve Time: 0.195509 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 2.25e-07 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00740406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209357 s | Solve Time: 0.217666 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 3.19e-08 ) ; ( R ) = ( 7.95e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0977278 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145449 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.51596e+08s, dt:5.78798e+06s, Cycle: 44 +wellControls: BHP (at the specified reference elevation): 28708824.107122038 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-01 ) ; ( Rwell ) = ( 3.19e-08 ) ; ( R ) = ( 3.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00943532 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226311 s | Solve Time: 0.173276 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 2.79e-06 ) ; ( R ) = ( 2.73e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00627439 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22734 s | Solve Time: 0.15372 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.20e-07 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.27e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00900097 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209605 s | Solve Time: 0.135484 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.78e-08 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.00e-03 ) ; +wellControls: BHP (at the specified reference elevation): 28726241.88047941 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.096223 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.138777 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.57384e+08s, dt:6.01293e+06s, Cycle: 45 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-01 ) ; ( Rwell ) = ( 1.78e-08 ) ; ( R ) = ( 3.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00803868 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214286 s | Solve Time: 0.141053 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-01 ) ; ( Rwell ) = ( 3.23e-06 ) ; ( R ) = ( 5.40e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-01 ) ; ( Rwell ) = ( 1.60e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00948404 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209961 s | Solve Time: 0.110243 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.85e-01 ) ; ( Rwell ) = ( 7.41e-07 ) ; ( R ) = ( 7.85e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 1.17e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00645653 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217936 s | Solve Time: 0.131042 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.79e-01 ) ; ( Rwell ) = ( 3.63e-07 ) ; ( R ) = ( 9.79e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-01 ) ; ( Rwell ) = ( 7.64e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-01 ) ; ( Rwell ) = ( 9.65e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 1.07e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00756233 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209133 s | Solve Time: 0.129695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 4.53e-07 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00975543 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205528 s | Solve Time: 0.0882452 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0984549 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100541 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.63397e+08s, dt:7.19994e+06s, Cycle: 46 +wellControls: BHP (at the specified reference elevation): 28743814.444668535 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00695871 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208379 s | Solve Time: 0.131169 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e+00 ) ; ( Rwell ) = ( 5.24e-07 ) ; ( R ) = ( 1.20e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 2.51e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00363591 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20977 s | Solve Time: 0.152092 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-01 ) ; ( Rwell ) = ( 1.36e-07 ) ; ( R ) = ( 2.31e-01 ) ; + Last LinSolve(iter,res) = ( 7, 3.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00583348 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208598 s | Solve Time: 0.110208 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 6.00e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00376893 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211036 s | Solve Time: 0.132557 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.117232 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.124171 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.70597e+08s, dt:7.87825e+06s, Cycle: 47 +wellControls: BHP (at the specified reference elevation): 28764875.91577168 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.67e-01 ) ; ( Rwell ) = ( 7.29e-09 ) ; ( R ) = ( 4.67e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00566082 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221975 s | Solve Time: 0.133404 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.03e-01 ) ; ( Rwell ) = ( 1.58e-06 ) ; ( R ) = ( 7.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 7.87e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00911272 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209694 s | Solve Time: 0.13236 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.68e-01 ) ; ( Rwell ) = ( 1.69e-07 ) ; ( R ) = ( 7.68e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 3.93e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 5.87e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00512475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208269 s | Solve Time: 0.152616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 1.95e-07 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00719503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209321 s | Solve Time: 0.109415 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.127896 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.140697 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.78475e+08s, dt:8.13037e+06s, Cycle: 48 +wellControls: BHP (at the specified reference elevation): 28788809.61465411 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-01 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 4.86e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00605562 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208124 s | Solve Time: 0.12967 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e+00 ) ; ( Rwell ) = ( 1.20e-06 ) ; ( R ) = ( 3.12e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 5.71e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00559908 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206132 s | Solve Time: 0.151266 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e+00 ) ; ( Rwell ) = ( 6.65e-07 ) ; ( R ) = ( 4.11e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e+00 ) ; ( Rwell ) = ( 6.04e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.11e-01 ) ; ( Rwell ) = ( 5.84e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-01 ) ; ( Rwell ) = ( 5.77e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 5.74e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00984596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218194 s | Solve Time: 0.137431 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-01 ) ; ( Rwell ) = ( 3.87e-07 ) ; ( R ) = ( 2.45e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00641184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215688 s | Solve Time: 0.176937 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00575897 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234881 s | Solve Time: 0.174891 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.63e-05 ) ; ( Rwell ) = ( 4.21e-09 ) ; ( R ) = ( 8.63e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.143628 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102241 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.86606e+08s, dt:9.66978e+06s, Cycle: 49 +wellControls: BHP (at the specified reference elevation): 28814392.436207715 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.58e-01 ) ; ( Rwell ) = ( 4.21e-09 ) ; ( R ) = ( 5.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00975518 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219361 s | Solve Time: 0.154105 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e+00 ) ; ( Rwell ) = ( 2.22e-06 ) ; ( R ) = ( 1.83e+00 ) ; + Last LinSolve(iter,res) = ( 7, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-01 ) ; ( Rwell ) = ( 1.11e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00542791 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220635 s | Solve Time: 0.174578 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-01 ) ; ( Rwell ) = ( 4.90e-07 ) ; ( R ) = ( 2.55e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00877754 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207716 s | Solve Time: 0.150586 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00540853 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206126 s | Solve Time: 0.174455 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.66e-04 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 3.66e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.159277 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.154665 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.96275e+08s, dt:9.52171e+06s, Cycle: 50 +wellControls: BHP (at the specified reference elevation): 28844107.3421959 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-01 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 5.38e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00622908 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208157 s | Solve Time: 0.195952 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e+00 ) ; ( Rwell ) = ( 2.01e-06 ) ; ( R ) = ( 2.89e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00657775 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208786 s | Solve Time: 0.194324 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e+00 ) ; ( Rwell ) = ( 9.91e-07 ) ; ( R ) = ( 3.23e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e+00 ) ; ( Rwell ) = ( 1.00e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00835869 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219268 s | Solve Time: 0.19752 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e+00 ) ; ( Rwell ) = ( 7.59e-07 ) ; ( R ) = ( 1.28e+00 ) ; + Last LinSolve(iter,res) = ( 9, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.55e-01 ) ; ( Rwell ) = ( 8.80e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 9.46e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 9.79e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00739798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229777 s | Solve Time: 0.176595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 9.96e-07 ) ; ( R ) = ( 3.13e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 9.86e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00711107 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209964 s | Solve Time: 0.198697 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 3.05e-07 ) ; ( R ) = ( 2.51e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 6.45e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00752758 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210508 s | Solve Time: 0.172197 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 4.37e-08 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 3.43e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00907993 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216217 s | Solve Time: 0.176185 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00947408 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207196 s | Solve Time: 0.153025 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.89e-04 ) ; ( Rwell ) = ( 7.30e-09 ) ; ( R ) = ( 1.89e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.163576 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.197243 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.05797e+08s, dt:8.22626e+06s, Cycle: 51 +wellControls: BHP (at the specified reference elevation): 28872492.017988868 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-01 ) ; ( Rwell ) = ( 7.30e-09 ) ; ( R ) = ( 4.78e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00693164 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206075 s | Solve Time: 0.172921 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.40e+00 ) ; ( Rwell ) = ( 3.58e-07 ) ; ( R ) = ( 2.40e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-01 ) ; ( Rwell ) = ( 1.75e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00610246 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21576 s | Solve Time: 0.151438 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.19e-01 ) ; ( Rwell ) = ( 8.13e-07 ) ; ( R ) = ( 6.19e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 3.92e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00667148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20651 s | Solve Time: 0.173267 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.24e-01 ) ; ( Rwell ) = ( 5.62e-07 ) ; ( R ) = ( 5.24e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 4.74e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 4.32e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00836821 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214486 s | Solve Time: 0.172887 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 2.74e-07 ) ; ( R ) = ( 3.19e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 3.53e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 3.93e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00690369 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206941 s | Solve Time: 0.154013 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.82e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 7.82e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0081741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20621 s | Solve Time: 0.116391 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.17e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.158654 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.148554 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.14023e+08s, dt:8.2661e+06s, Cycle: 52 +wellControls: BHP (at the specified reference elevation): 28897948.806972142 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-01 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 4.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0082804 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215771 s | Solve Time: 0.132879 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e+00 ) ; ( Rwell ) = ( 7.90e-07 ) ; ( R ) = ( 1.57e+00 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.02e-01 ) ; ( Rwell ) = ( 4.04e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-01 ) ; ( Rwell ) = ( 2.11e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00602467 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215602 s | Solve Time: 0.160384 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-01 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 3.97e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 4.24e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00979862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.231368 s | Solve Time: 0.132997 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 5.87e-07 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00750952 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21568 s | Solve Time: 0.0920458 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 6.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.145731 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132593 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.22289e+08s, dt:8.77527e+06s, Cycle: 53 +wellControls: BHP (at the specified reference elevation): 28923471.978887256 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-01 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 5.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0074444 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214297 s | Solve Time: 0.139239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e+00 ) ; ( Rwell ) = ( 6.09e-07 ) ; ( R ) = ( 1.12e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 2.17e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0047854 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207407 s | Solve Time: 0.152575 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e+00 ) ; ( Rwell ) = ( 2.68e-07 ) ; ( R ) = ( 1.24e+00 ) ; + Last LinSolve(iter,res) = ( 7, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-01 ) ; ( Rwell ) = ( 1.20e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0085921 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208371 s | Solve Time: 0.17397 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 2.17e-07 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 8, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.08e-01 ) ; ( Rwell ) = ( 1.15e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 9.72e-08 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00888682 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206379 s | Solve Time: 0.173321 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.24e-02 ) ; ( Rwell ) = ( 5.23e-07 ) ; ( R ) = ( 9.24e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00660165 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206968 s | Solve Time: 0.175146 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.140337 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.151818 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.31065e+08s, dt:8.72241e+06s, Cycle: 54 +wellControls: BHP (at the specified reference elevation): 28949368.03301757 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-01 ) ; ( Rwell ) = ( 7.76e-09 ) ; ( R ) = ( 5.04e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00579235 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208895 s | Solve Time: 0.20176 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.20e-01 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 9.20e-01 ) ; + Last LinSolve(iter,res) = ( 9, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-01 ) ; ( Rwell ) = ( 5.91e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00710213 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209644 s | Solve Time: 0.219022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.30e-01 ) ; ( Rwell ) = ( 1.44e-07 ) ; ( R ) = ( 6.30e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 3.53e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00674766 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207623 s | Solve Time: 0.152373 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 2.88e-07 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00973642 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229774 s | Solve Time: 0.131385 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 5.61e-08 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00670124 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222896 s | Solve Time: 0.172764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.70e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.15784 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.169762 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.39787e+08s, dt:8.18335e+06s, Cycle: 55 +wellControls: BHP (at the specified reference elevation): 28976741.096728947 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-01 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 4.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00707301 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219903 s | Solve Time: 0.151468 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e+00 ) ; ( Rwell ) = ( 6.13e-07 ) ; ( R ) = ( 2.03e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-01 ) ; ( Rwell ) = ( 3.00e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 1.45e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00485753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228178 s | Solve Time: 0.173145 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.34e-01 ) ; ( Rwell ) = ( 4.30e-07 ) ; ( R ) = ( 6.34e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 1.57e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00747231 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207131 s | Solve Time: 0.151197 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e+00 ) ; ( Rwell ) = ( 4.77e-07 ) ; ( R ) = ( 1.29e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 1.78e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00600449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208756 s | Solve Time: 0.175844 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-01 ) ; ( Rwell ) = ( 4.11e-07 ) ; ( R ) = ( 2.27e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 1.28e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00699858 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208508 s | Solve Time: 0.193538 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 1.37e-07 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00709052 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206375 s | Solve Time: 0.0889224 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.139417 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.178663 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.4797e+08s, dt:7.46969e+06s, Cycle: 56 +wellControls: BHP (at the specified reference elevation): 29002386.10796534 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 6.69e-09 ) ; ( R ) = ( 4.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00474808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208073 s | Solve Time: 0.132894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-01 ) ; ( Rwell ) = ( 1.21e-06 ) ; ( R ) = ( 3.55e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00978495 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21004 s | Solve Time: 0.109578 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 1.39e-07 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00528011 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221951 s | Solve Time: 0.111627 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00846534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209409 s | Solve Time: 0.110082 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.21e-05 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 8.21e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.119142 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.131197 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.5544e+08s, dt:7.96917e+06s, Cycle: 57 +wellControls: BHP (at the specified reference elevation): 29026035.150980975 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-01 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 4.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00739544 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205316 s | Solve Time: 0.130539 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.18e+00 ) ; ( Rwell ) = ( 6.05e-07 ) ; ( R ) = ( 4.18e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e+00 ) ; ( Rwell ) = ( 3.01e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 1.50e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00656207 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207897 s | Solve Time: 0.152371 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.00e+00 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 4.00e+00 ) ; + Last LinSolve(iter,res) = ( 7, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e+00 ) ; ( Rwell ) = ( 8.69e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-01 ) ; ( Rwell ) = ( 3.66e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-01 ) ; ( Rwell ) = ( 1.20e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 4.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00700053 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20667 s | Solve Time: 0.150803 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.40e-01 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 4.40e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 5.09e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00775857 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20741 s | Solve Time: 0.151885 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.24e-01 ) ; ( Rwell ) = ( 1.74e-06 ) ; ( R ) = ( 4.24e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 6.28e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00551907 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.232115 s | Solve Time: 0.153224 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 7.18e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00496294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206788 s | Solve Time: 0.130448 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; ( R ) = ( 6.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.132029 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.150516 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.63409e+08s, dt:7.9555e+06s, Cycle: 58 +wellControls: BHP (at the specified reference elevation): 29049948.0742736 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-01 ) ; ( Rwell ) = ( 2.46e-09 ) ; ( R ) = ( 4.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00687966 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207114 s | Solve Time: 0.13283 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.17e-01 ) ; ( Rwell ) = ( 1.02e-06 ) ; ( R ) = ( 5.17e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-01 ) ; ( Rwell ) = ( 5.08e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00776134 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209316 s | Solve Time: 0.131823 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 7.42e-07 ) ; ( R ) = ( 2.32e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00788683 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211179 s | Solve Time: 0.111522 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 6.52e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00615546 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210262 s | Solve Time: 0.110283 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 5.97e-09 ) ; ( R ) = ( 7.46e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.131654 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0905027 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.71365e+08s, dt:1.67522e+06s, Cycle: 59 +wellControls: BHP (at the specified reference elevation): 29073614.477042817 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.25e-02 ) ; ( Rwell ) = ( 5.97e-09 ) ; ( R ) = ( 9.25e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00476953 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211459 s | Solve Time: 0.0889351 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.24e-06 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00721693 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220736 s | Solve Time: 0.131021 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.034536 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0500313 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.7304e+08s, dt:2.51244e+06s, Cycle: 60 +wellControls: BHP (at the specified reference elevation): 29079263.747793656 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.16677e+07, 2.83869e+07, 4.00598e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.08468e+06, 2.0039e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45759e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.89344e+07, 3.4547e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 1.85059e+10, 3.35501e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00735e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1.85059e+10, 0 }, { 4.90278e+09, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 1.47e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00499217 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207422 s | Solve Time: 0.0905906 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 1.02e-06 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00514359 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21155 s | Solve Time: 0.132451 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 8.01e-09 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00641521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206441 s | Solve Time: 0.109367 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 7.00e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0469201 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.136392 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.75552e+08s, dt:2.63182e+06s, Cycle: 61 +wellControls: BHP (at the specified reference elevation): 29087287.7416489 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 1.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00492881 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206683 s | Solve Time: 0.0895834 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e+00 ) ; ( Rwell ) = ( 1.91e-06 ) ; ( R ) = ( 2.94e+00 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e+00 ) ; ( Rwell ) = ( 9.55e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 4.77e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 2.38e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0091425 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212332 s | Solve Time: 0.0938991 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.27e+00 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 3.27e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e+00 ) ; ( Rwell ) = ( 1.01e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.45e-01 ) ; ( Rwell ) = ( 6.24e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-01 ) ; ( Rwell ) = ( 4.30e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 3.34e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00429821 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229275 s | Solve Time: 0.110388 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.39e+00 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 3.39e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e+00 ) ; ( Rwell ) = ( 7.03e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-01 ) ; ( Rwell ) = ( 5.18e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-01 ) ; ( Rwell ) = ( 4.26e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 3.80e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0044852 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222346 s | Solve Time: 0.108812 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 9.88e-07 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00896657 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207948 s | Solve Time: 0.0883927 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00663743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206277 s | Solve Time: 0.111261 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.10e-04 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 3.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0567281 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133815 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.78184e+08s, dt:2.78191e+06s, Cycle: 62 +wellControls: BHP (at the specified reference elevation): 29095605.66760591 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 2.14e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00467158 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208366 s | Solve Time: 0.089373 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 4.17e-07 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00712377 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223799 s | Solve Time: 0.108796 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 9.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00885443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224725 s | Solve Time: 0.0713731 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0496773 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.149152 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.80966e+08s, dt:2.78979e+06s, Cycle: 63 +wellControls: BHP (at the specified reference elevation): 29104260.54119625 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 2.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00879099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2064 s | Solve Time: 0.0888746 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.70e-06 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00987763 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208297 s | Solve Time: 0.110056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0517591 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0827957 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.83756e+08s, dt:3.59515e+06s, Cycle: 64 +wellControls: BHP (at the specified reference elevation): 29113069.297308516 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 2.33e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00884311 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205982 s | Solve Time: 0.0880674 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.58e-01 ) ; ( Rwell ) = ( 5.95e-07 ) ; ( R ) = ( 6.58e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 3.09e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 1.68e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00744253 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229065 s | Solve Time: 0.116495 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.14e-02 ) ; ( Rwell ) = ( 3.22e-07 ) ; ( R ) = ( 8.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00427765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210362 s | Solve Time: 0.13472 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.28e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0631518 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0946119 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.87351e+08s, dt:4.40921e+06s, Cycle: 65 +wellControls: BHP (at the specified reference elevation): 29124703.628385548 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 2.92e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0091546 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212994 s | Solve Time: 0.0904973 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 2.62e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00642454 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219722 s | Solve Time: 0.111703 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00678448 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215993 s | Solve Time: 0.110075 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0746383 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.125728 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.9176e+08s, dt:4.79735e+06s, Cycle: 66 +wellControls: BHP (at the specified reference elevation): 29138222.84044096 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 3.24e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00579286 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219784 s | Solve Time: 0.109116 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.40e-01 ) ; ( Rwell ) = ( 4.65e-07 ) ; ( R ) = ( 2.40e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00687501 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208677 s | Solve Time: 0.129887 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 8.03e-08 ) ; ( R ) = ( 1.54e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00364071 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207956 s | Solve Time: 0.0889626 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00703722 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206741 s | Solve Time: 0.0683291 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 8.29e-09 ) ; ( R ) = ( 4.31e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.08817 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.121348 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.96558e+08s, dt:5.3039e+06s, Cycle: 67 +wellControls: BHP (at the specified reference elevation): 29153096.914843474 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 8.29e-09 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00918094 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204518 s | Solve Time: 0.116212 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.52e-01 ) ; ( Rwell ) = ( 4.46e-07 ) ; ( R ) = ( 6.52e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 2.21e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00848521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206459 s | Solve Time: 0.130463 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e-01 ) ; ( Rwell ) = ( 1.36e-06 ) ; ( R ) = ( 5.88e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 7.08e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 4.04e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00444652 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225454 s | Solve Time: 0.135625 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 8.22e-07 ) ; ( R ) = ( 4.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 5.99e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00411687 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208739 s | Solve Time: 0.131172 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.45e-02 ) ; ( Rwell ) = ( 5.37e-07 ) ; ( R ) = ( 8.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00395537 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212488 s | Solve Time: 0.0895693 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.68e-08 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0993842 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.146735 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.01862e+08s, dt:5.36227e+06s, Cycle: 68 +wellControls: BHP (at the specified reference elevation): 29169313.64557136 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-01 ) ; ( Rwell ) = ( 1.68e-08 ) ; ( R ) = ( 3.63e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00682489 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208536 s | Solve Time: 0.131136 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.73e+01 ) ; ( Rwell ) = ( 2.18e-06 ) ; ( R ) = ( 7.73e+01 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-01 ) ; ( Rwell ) = ( 1.10e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00884816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207859 s | Solve Time: 0.10908 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 8.21e-07 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.008441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207332 s | Solve Time: 0.130347 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00924795 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205989 s | Solve Time: 0.1317 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.92e-04 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 2.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.25e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0859248 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.1456 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.07224e+08s, dt:5.44208e+06s, Cycle: 69 +wellControls: BHP (at the specified reference elevation): 29185517.27483693 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-01 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 3.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00893486 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206313 s | Solve Time: 0.135148 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e+01 ) ; ( Rwell ) = ( 6.30e-07 ) ; ( R ) = ( 2.47e+01 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.35e+00 ) ; ( Rwell ) = ( 3.18e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 1.63e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00439765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216282 s | Solve Time: 0.153952 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e+01 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 2.04e+01 ) ; + Last LinSolve(iter,res) = ( 7, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.50e+00 ) ; ( Rwell ) = ( 3.41e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e+00 ) ; ( Rwell ) = ( 2.49e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e+00 ) ; ( Rwell ) = ( 2.04e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-01 ) ; ( Rwell ) = ( 1.83e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00411689 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206756 s | Solve Time: 0.172695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 4.58e-07 ) ; ( R ) = ( 1.82e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00664717 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218954 s | Solve Time: 0.151166 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00643556 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21533 s | Solve Time: 0.173853 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.10885 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.114713 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.12666e+08s, dt:6.16754e+06s, Cycle: 70 +wellControls: BHP (at the specified reference elevation): 29201947.653889954 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-01 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 3.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00906349 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222425 s | Solve Time: 0.172044 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e+00 ) ; ( Rwell ) = ( 1.75e-06 ) ; ( R ) = ( 1.41e+00 ) ; + Last LinSolve(iter,res) = ( 8, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 8.74e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00874414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207734 s | Solve Time: 0.172773 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 3.13e-07 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00855416 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207269 s | Solve Time: 0.130456 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 1.35e-07 ) ; ( R ) = ( 3.08e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00886026 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207729 s | Solve Time: 0.110528 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.79e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.86e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.102059 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100823 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.18833e+08s, dt:7.37676e+06s, Cycle: 71 +wellControls: BHP (at the specified reference elevation): 29221865.23835165 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-01 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 4.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00398319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211734 s | Solve Time: 0.173079 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e+00 ) ; ( Rwell ) = ( 1.34e-06 ) ; ( R ) = ( 1.34e+00 ) ; + Last LinSolve(iter,res) = ( 8, 3.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-01 ) ; ( Rwell ) = ( 6.66e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00954494 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219276 s | Solve Time: 0.15749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.35e-01 ) ; ( Rwell ) = ( 2.35e-06 ) ; ( R ) = ( 4.35e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 8.49e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00395778 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206775 s | Solve Time: 0.175717 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 5.12e-07 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 8, 3.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00953797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207074 s | Solve Time: 0.131987 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.89e-03 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 7.89e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.130666 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.174601 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 5.2621e+08s, dt:6.81768e+06s, Cycle: 72 +wellControls: BHP (at the specified reference elevation): 29244630.52964307 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-01 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 4.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0087855 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220303 s | Solve Time: 0.156018 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.80e-01 ) ; ( Rwell ) = ( 3.49e-06 ) ; ( R ) = ( 7.80e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 1.80e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0088239 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217864 s | Solve Time: 0.15244 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.38e-01 ) ; ( Rwell ) = ( 2.27e-06 ) ; ( R ) = ( 8.38e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 2.04e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00668863 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2121 s | Solve Time: 0.152024 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 1.10e-06 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00601671 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209239 s | Solve Time: 0.109856 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.23e-03 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 8.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.118097 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.130087 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.33028e+08s, dt:7.30239e+06s, Cycle: 73 +wellControls: BHP (at the specified reference elevation): 29267093.226152845 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-01 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 4.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00924757 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.231299 s | Solve Time: 0.153077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e+00 ) ; ( Rwell ) = ( 7.44e-07 ) ; ( R ) = ( 4.38e+00 ) ; + Last LinSolve(iter,res) = ( 7, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-01 ) ; ( Rwell ) = ( 3.92e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 2.17e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00437063 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21367 s | Solve Time: 0.172344 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.31e-01 ) ; ( Rwell ) = ( 1.30e-06 ) ; ( R ) = ( 7.31e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 5.52e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00466193 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220184 s | Solve Time: 0.175177 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.33e-01 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 4.33e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 1.14e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00459596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.232876 s | Solve Time: 0.173713 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 8.42e-07 ) ; ( R ) = ( 3.94e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-02 ) ; ( Rwell ) = ( 9.90e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00459072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210277 s | Solve Time: 0.172822 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.04e-01 ) ; ( Rwell ) = ( 4.15e-07 ) ; ( R ) = ( 4.04e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 7.02e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-02 ) ; ( Rwell ) = ( 8.46e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00491501 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207942 s | Solve Time: 0.176719 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 3.19e-07 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00929057 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208396 s | Solve Time: 0.13016 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 7.07e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.124183 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.134279 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.4033e+08s, dt:7.70622e+06s, Cycle: 74 +wellControls: BHP (at the specified reference elevation): 29290339.415509112 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-01 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 5.19e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00466358 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207741 s | Solve Time: 0.174847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e+00 ) ; ( Rwell ) = ( 4.24e-06 ) ; ( R ) = ( 1.62e+00 ) ; + Last LinSolve(iter,res) = ( 8, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-01 ) ; ( Rwell ) = ( 2.12e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00838622 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210963 s | Solve Time: 0.159588 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.81e-01 ) ; ( Rwell ) = ( 6.04e-06 ) ; ( R ) = ( 6.81e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 1.96e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00946808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222228 s | Solve Time: 0.153329 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 3.49e-06 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.47e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00821466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207646 s | Solve Time: 0.153297 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 6.32e-08 ) ; ( R ) = ( 6.11e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.21e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.125388 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.162266 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 5.48037e+08s, dt:7.40352e+06s, Cycle: 75 +wellControls: BHP (at the specified reference elevation): 29313827.4055191 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-01 ) ; ( Rwell ) = ( 6.32e-08 ) ; ( R ) = ( 5.02e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00400428 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217333 s | Solve Time: 0.194405 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e+00 ) ; ( Rwell ) = ( 2.01e-07 ) ; ( R ) = ( 2.10e+00 ) ; + Last LinSolve(iter,res) = ( 9, 4.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-01 ) ; ( Rwell ) = ( 9.90e-08 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00491992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212066 s | Solve Time: 0.220667 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e+00 ) ; ( Rwell ) = ( 1.41e-06 ) ; ( R ) = ( 2.25e+00 ) ; + Last LinSolve(iter,res) = ( 10, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-01 ) ; ( Rwell ) = ( 6.75e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-01 ) ; ( Rwell ) = ( 3.10e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.92e-01 ) ; ( Rwell ) = ( 1.36e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00900842 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227571 s | Solve Time: 0.199766 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-01 ) ; ( Rwell ) = ( 3.53e-07 ) ; ( R ) = ( 3.21e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00852512 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.23006 s | Solve Time: 0.174339 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.44e-07 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00890857 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223279 s | Solve Time: 0.151707 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.122877 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132636 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.5544e+08s, dt:7.85836e+06s, Cycle: 76 +wellControls: BHP (at the specified reference elevation): 29336430.732285623 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-01 ) ; ( Rwell ) = ( 3.81e-09 ) ; ( R ) = ( 5.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00868154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20654 s | Solve Time: 0.193676 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e+00 ) ; ( Rwell ) = ( 7.74e-06 ) ; ( R ) = ( 1.41e+00 ) ; + Last LinSolve(iter,res) = ( 9, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-01 ) ; ( Rwell ) = ( 3.87e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00400426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.235237 s | Solve Time: 0.222766 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 1.42e-06 ) ; ( R ) = ( 4.00e-01 ) ; + Last LinSolve(iter,res) = ( 10, 4.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00811573 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209563 s | Solve Time: 0.179201 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.61e-07 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00520377 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207139 s | Solve Time: 0.13023 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 9.95e-09 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.129564 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.163564 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 5.63298e+08s, dt:7.51843e+06s, Cycle: 77 +wellControls: BHP (at the specified reference elevation): 29360669.475889932 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 9.95e-09 ) ; ( R ) = ( 4.84e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00547858 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206876 s | Solve Time: 0.214579 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-01 ) ; ( Rwell ) = ( 4.00e-06 ) ; ( R ) = ( 5.52e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 2.00e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.00625488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209145 s | Solve Time: 0.345637 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 8.54e-07 ) ; ( R ) = ( 1.90e-01 ) ; + Last LinSolve(iter,res) = ( 16, 6.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00749639 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207342 s | Solve Time: 0.130781 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 1.85e-07 ) ; ( R ) = ( 7.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00450719 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20759 s | Solve Time: 0.304298 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.50e-08 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 14, 4.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.126829 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.146396 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.70817e+08s, dt:7.60986e+06s, Cycle: 78 +wellControls: BHP (at the specified reference elevation): 29383237.731309753 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-01 ) ; ( Rwell ) = ( 2.50e-08 ) ; ( R ) = ( 4.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 16 | Final Rel Res: 0.0066344 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217625 s | Solve Time: 0.345309 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e+00 ) ; ( Rwell ) = ( 7.89e-06 ) ; ( R ) = ( 3.29e+00 ) ; + Last LinSolve(iter,res) = ( 16, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e+00 ) ; ( Rwell ) = ( 3.93e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-01 ) ; ( Rwell ) = ( 1.95e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00899616 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220392 s | Solve Time: 0.238912 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.84e-01 ) ; ( Rwell ) = ( 3.93e-07 ) ; ( R ) = ( 6.84e-01 ) ; + Last LinSolve(iter,res) = ( 11, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 1.17e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00668439 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215249 s | Solve Time: 0.172555 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 6.67e-07 ) ; ( R ) = ( 3.78e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 9.19e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00533478 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213206 s | Solve Time: 0.173694 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.11e-01 ) ; ( Rwell ) = ( 1.60e-07 ) ; ( R ) = ( 3.11e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 5.37e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00859988 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213953 s | Solve Time: 0.153695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 6.62e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00749433 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217161 s | Solve Time: 0.136917 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.120905 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.139733 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.78427e+08s, dt:7.87951e+06s, Cycle: 79 +wellControls: BHP (at the specified reference elevation): 29406340.43818274 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-01 ) ; ( Rwell ) = ( 6.82e-09 ) ; ( R ) = ( 5.03e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00460793 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209335 s | Solve Time: 0.174681 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e+00 ) ; ( Rwell ) = ( 2.45e-07 ) ; ( R ) = ( 1.37e+00 ) ; + Last LinSolve(iter,res) = ( 8, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-01 ) ; ( Rwell ) = ( 1.21e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00726381 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209198 s | Solve Time: 0.19765 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; ( R ) = ( 3.44e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00305432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234539 s | Solve Time: 0.152337 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 8.16e-08 ) ; ( R ) = ( 4.82e-01 ) ; + Last LinSolve(iter,res) = ( 7, 3.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 4.73e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00425115 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206872 s | Solve Time: 0.151949 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00826875 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220983 s | Solve Time: 0.0899787 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.137767 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.202988 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 5.86306e+08s, dt:6.6967e+06s, Cycle: 80 +wellControls: BHP (at the specified reference elevation): 29430041.558903992 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-01 ) ; ( Rwell ) = ( 7.64e-09 ) ; ( R ) = ( 4.75e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00819086 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218506 s | Solve Time: 0.152881 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e+00 ) ; ( Rwell ) = ( 1.61e-06 ) ; ( R ) = ( 3.96e+00 ) ; + Last LinSolve(iter,res) = ( 7, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.33e-01 ) ; ( Rwell ) = ( 8.03e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-01 ) ; ( Rwell ) = ( 4.01e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00826596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206743 s | Solve Time: 0.151167 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e+00 ) ; ( Rwell ) = ( 8.20e-07 ) ; ( R ) = ( 1.77e+00 ) ; + Last LinSolve(iter,res) = ( 7, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.85e-01 ) ; ( Rwell ) = ( 6.09e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-01 ) ; ( Rwell ) = ( 5.04e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00847848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218355 s | Solve Time: 0.151049 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 6.50e-07 ) ; ( R ) = ( 3.65e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 5.76e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00729051 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205487 s | Solve Time: 0.151052 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0077908 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224812 s | Solve Time: 0.132212 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 8.57e-08 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00813409 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227957 s | Solve Time: 0.113573 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.86e-04 ) ; ( Rwell ) = ( 6.01e-09 ) ; ( R ) = ( 1.86e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.113008 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.154115 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 5.93003e+08s, dt:6.60609e+06s, Cycle: 81 +wellControls: BHP (at the specified reference elevation): 29451296.026575774 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-01 ) ; ( Rwell ) = ( 6.01e-09 ) ; ( R ) = ( 4.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00726547 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215352 s | Solve Time: 0.151296 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.91e-01 ) ; ( Rwell ) = ( 4.14e-07 ) ; ( R ) = ( 5.91e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 2.09e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00830657 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209358 s | Solve Time: 0.152004 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-01 ) ; ( Rwell ) = ( 1.85e-07 ) ; ( R ) = ( 2.47e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00686304 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20827 s | Solve Time: 0.129735 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.48e-07 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00538161 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213823 s | Solve Time: 0.11109 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 4.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.109816 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132993 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.99609e+08s, dt:7.00309e+06s, Cycle: 82 +wellControls: BHP (at the specified reference elevation): 29472466.594435748 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-01 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 5.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00879026 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208501 s | Solve Time: 0.150663 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.63e-01 ) ; ( Rwell ) = ( 3.74e-07 ) ; ( R ) = ( 9.63e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-01 ) ; ( Rwell ) = ( 1.87e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0093294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209854 s | Solve Time: 0.151331 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 4.78e-07 ) ; ( R ) = ( 3.06e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0048876 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205722 s | Solve Time: 0.130695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 3.01e-08 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00711456 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214709 s | Solve Time: 0.0909274 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.115808 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.122513 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.06612e+08s, dt:7.70945e+06s, Cycle: 83 +wellControls: BHP (at the specified reference elevation): 29494245.137964923 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.88e-01 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 5.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00521203 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21738 s | Solve Time: 0.172436 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.40e-01 ) ; ( Rwell ) = ( 5.16e-07 ) ; ( R ) = ( 8.40e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-01 ) ; ( Rwell ) = ( 2.44e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00547635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215509 s | Solve Time: 0.172113 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 3.43e-07 ) ; ( R ) = ( 4.17e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 2.92e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00689206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229025 s | Solve Time: 0.172986 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 3.05e-07 ) ; ( R ) = ( 2.44e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00729273 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213778 s | Solve Time: 0.114894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 1.80e-07 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00882745 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211547 s | Solve Time: 0.131869 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.145394 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.197612 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 6.14322e+08s, dt:6.65349e+06s, Cycle: 84 +wellControls: BHP (at the specified reference elevation): 29518608.63962836 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-01 ) ; ( Rwell ) = ( 4.42e-09 ) ; ( R ) = ( 5.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00891894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20866 s | Solve Time: 0.151824 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.78e+00 ) ; ( Rwell ) = ( 5.14e-07 ) ; ( R ) = ( 2.78e+00 ) ; + Last LinSolve(iter,res) = ( 7, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-01 ) ; ( Rwell ) = ( 2.56e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-01 ) ; ( Rwell ) = ( 1.27e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00955172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207107 s | Solve Time: 0.155229 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-01 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 5.03e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 8.01e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00586585 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206292 s | Solve Time: 0.152266 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 3.83e-07 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00559181 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205577 s | Solve Time: 0.151108 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 6.88e-08 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00725925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207237 s | Solve Time: 0.088661 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.86e-04 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 1.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.119271 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.162572 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 6.20975e+08s, dt:6.38589e+06s, Cycle: 85 +wellControls: BHP (at the specified reference elevation): 29539613.982973967 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-01 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 5.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00693153 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205443 s | Solve Time: 0.151317 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.65e-01 ) ; ( Rwell ) = ( 5.71e-06 ) ; ( R ) = ( 6.65e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 2.85e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00928728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223978 s | Solve Time: 0.154141 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 5.08e-06 ) ; ( R ) = ( 3.10e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 3.96e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00845256 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207736 s | Solve Time: 0.151527 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.85e-02 ) ; ( Rwell ) = ( 3.34e-06 ) ; ( R ) = ( 8.85e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00676367 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205763 s | Solve Time: 0.129738 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 2.04e-08 ) ; ( R ) = ( 5.66e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.106507 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.148635 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.27361e+08s, dt:3.35908e+06s, Cycle: 86 +wellControls: BHP (at the specified reference elevation): 29559733.205644164 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 2.04e-08 ) ; ( R ) = ( 2.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00742422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205238 s | Solve Time: 0.129369 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 6.65e-06 ) ; ( R ) = ( 2.19e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00550432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206034 s | Solve Time: 0.0898824 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.03e-07 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00725633 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214319 s | Solve Time: 0.0899764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.27e-04 ) ; ( Rwell ) = ( 2.09e-08 ) ; ( R ) = ( 3.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.053363 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.071048 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.3072e+08s, dt:4.55884e+06s, Cycle: 87 +wellControls: BHP (at the specified reference elevation): 29570236.35730114 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.22031e+07, 2.89224e+07, 4.05881e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.60396e+06, 2.51231e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45778e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.88119e+07, 3.4539e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.51128e+10, 3.35506e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00766e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.51128e+10, 0 }, { 6.09912e+09, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.47e-01 ) ; ( Rwell ) = ( 2.09e-08 ) ; ( R ) = ( 3.47e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00392907 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234495 s | Solve Time: 0.152948 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 5.90e-06 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 7, 3.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00534042 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213518 s | Solve Time: 0.151049 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 9.64e-08 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00583929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206473 s | Solve Time: 0.110989 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-04 ) ; ( Rwell ) = ( 2.69e-08 ) ; ( R ) = ( 3.37e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0737912 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0734761 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.35279e+08s, dt:6.1199e+06s, Cycle: 88 +wellControls: BHP (at the specified reference elevation): 29584471.612029493 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-01 ) ; ( Rwell ) = ( 2.69e-08 ) ; ( R ) = ( 4.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00617152 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205546 s | Solve Time: 0.155193 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e+00 ) ; ( Rwell ) = ( 7.39e-07 ) ; ( R ) = ( 1.76e+00 ) ; + Last LinSolve(iter,res) = ( 7, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-01 ) ; ( Rwell ) = ( 3.58e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 1.68e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0066139 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222995 s | Solve Time: 0.151788 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.24e-01 ) ; ( Rwell ) = ( 9.70e-07 ) ; ( R ) = ( 9.24e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-01 ) ; ( Rwell ) = ( 5.63e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 3.61e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0099649 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207907 s | Solve Time: 0.155668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 4.22e-06 ) ; ( R ) = ( 3.79e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 2.29e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00934244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205791 s | Solve Time: 0.151488 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 2.25e-06 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00505091 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22384 s | Solve Time: 0.129992 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0069485 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225814 s | Solve Time: 0.110247 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.61e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 1.61e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0970825 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.201963 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 6.41399e+08s, dt:5.21638e+06s, Cycle: 89 +wellControls: BHP (at the specified reference elevation): 29603892.457814537 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-01 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 4.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00518657 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205946 s | Solve Time: 0.150871 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.59e-01 ) ; ( Rwell ) = ( 4.96e-06 ) ; ( R ) = ( 9.59e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 2.48e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00774764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205813 s | Solve Time: 0.150775 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 3.24e-06 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0096625 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2066 s | Solve Time: 0.153407 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 8.50e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0849818 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12269 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.46615e+08s, dt:5.73879e+06s, Cycle: 90 +wellControls: BHP (at the specified reference elevation): 29620874.458617132 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-01 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 4.47e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00968159 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206637 s | Solve Time: 0.219249 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 1.72e-05 ) ; ( R ) = ( 4.00e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00321728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205062 s | Solve Time: 0.151403 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 7, 3.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00899857 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206965 s | Solve Time: 0.108294 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0888985 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12642 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.52354e+08s, dt:6.22834e+06s, Cycle: 91 +wellControls: BHP (at the specified reference elevation): 29639070.130034026 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 4.84e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0081256 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207097 s | Solve Time: 0.151461 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.71e-01 ) ; ( Rwell ) = ( 7.38e-06 ) ; ( R ) = ( 9.71e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-01 ) ; ( Rwell ) = ( 3.69e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00970796 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218725 s | Solve Time: 0.153285 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 3.96e-06 ) ; ( R ) = ( 1.89e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00768954 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207021 s | Solve Time: 0.129717 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 9.71e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844714 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222764 s | Solve Time: 0.114725 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.75e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 2.75e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.100286 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.118985 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.58582e+08s, dt:6.9465e+06s, Cycle: 92 +wellControls: BHP (at the specified reference elevation): 29658760.191837262 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-01 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 5.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00450709 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210628 s | Solve Time: 0.173626 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-01 ) ; ( Rwell ) = ( 5.65e-06 ) ; ( R ) = ( 5.25e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.51e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00394243 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209435 s | Solve Time: 0.152616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 7.73e-07 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 7, 3.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00914927 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210894 s | Solve Time: 0.0889755 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 8.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.128991 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.141333 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.65529e+08s, dt:7.15316e+06s, Cycle: 93 +wellControls: BHP (at the specified reference elevation): 29681119.63681883 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-01 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 5.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00509348 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227107 s | Solve Time: 0.174273 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e+00 ) ; ( Rwell ) = ( 6.26e-06 ) ; ( R ) = ( 1.61e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 3.15e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00432346 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.240065 s | Solve Time: 0.17493 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 3.28e-06 ) ; ( R ) = ( 1.88e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0080686 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208206 s | Solve Time: 0.109234 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 3.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00619582 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212233 s | Solve Time: 0.113691 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 7.67e-09 ) ; ( R ) = ( 5.40e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.116026 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.148023 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.72682e+08s, dt:7.2006e+06s, Cycle: 94 +wellControls: BHP (at the specified reference elevation): 29703531.08388145 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.50e-01 ) ; ( Rwell ) = ( 7.67e-09 ) ; ( R ) = ( 5.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00511503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207513 s | Solve Time: 0.177434 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e+00 ) ; ( Rwell ) = ( 6.27e-06 ) ; ( R ) = ( 1.75e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-01 ) ; ( Rwell ) = ( 3.13e-06 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00535089 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.23307 s | Solve Time: 0.183441 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e-01 ) ; ( Rwell ) = ( 3.28e-06 ) ; ( R ) = ( 4.11e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0058953 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21216 s | Solve Time: 0.152347 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 2.05e-07 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0086878 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211637 s | Solve Time: 0.110415 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.109393 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.112135 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.79883e+08s, dt:8.24071e+06s, Cycle: 95 +wellControls: BHP (at the specified reference elevation): 29725613.31403797 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-01 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 6.02e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00632857 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210225 s | Solve Time: 0.194867 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.32e-01 ) ; ( Rwell ) = ( 1.74e-06 ) ; ( R ) = ( 6.32e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 8.63e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0057876 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206937 s | Solve Time: 0.172098 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 2.27e-07 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00427506 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234111 s | Solve Time: 0.156552 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00839499 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212918 s | Solve Time: 0.109135 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; ( R ) = ( 4.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.124363 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145259 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.88123e+08s, dt:8.37304e+06s, Cycle: 96 +wellControls: BHP (at the specified reference elevation): 29750519.198401075 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-01 ) ; ( Rwell ) = ( 3.40e-09 ) ; ( R ) = ( 5.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00706842 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215189 s | Solve Time: 0.177117 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.91e-01 ) ; ( Rwell ) = ( 4.03e-07 ) ; ( R ) = ( 7.91e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-01 ) ; ( Rwell ) = ( 2.01e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00674798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230536 s | Solve Time: 0.173522 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 5.83e-07 ) ; ( R ) = ( 2.39e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00445742 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225558 s | Solve Time: 0.152894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 5.21e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00674785 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221734 s | Solve Time: 0.116503 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.127948 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.167283 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 6.96496e+08s, dt:7.91694e+06s, Cycle: 97 +wellControls: BHP (at the specified reference elevation): 29776236.33513583 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.49e-01 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 5.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00565779 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223494 s | Solve Time: 0.176137 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e+00 ) ; ( Rwell ) = ( 6.18e-07 ) ; ( R ) = ( 2.39e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 3.01e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00740803 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206995 s | Solve Time: 0.173769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 4.96e-07 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00596152 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211398 s | Solve Time: 0.15364 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00803974 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213476 s | Solve Time: 0.109618 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.132189 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.117404 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.04413e+08s, dt:8.88199e+06s, Cycle: 98 +wellControls: BHP (at the specified reference elevation): 29801570.849503323 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.88e-01 ) ; ( Rwell ) = ( 4.66e-09 ) ; ( R ) = ( 5.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00424525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205075 s | Solve Time: 0.192982 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.49e-01 ) ; ( Rwell ) = ( 2.75e-07 ) ; ( R ) = ( 6.49e-01 ) ; + Last LinSolve(iter,res) = ( 9, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-01 ) ; ( Rwell ) = ( 1.36e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00442247 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207428 s | Solve Time: 0.199028 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 9.02e-08 ) ; ( R ) = ( 2.72e-01 ) ; + Last LinSolve(iter,res) = ( 9, 4.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00881108 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209097 s | Solve Time: 0.160475 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00797674 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208769 s | Solve Time: 0.153495 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.151702 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.149749 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.13295e+08s, dt:8.88943e+06s, Cycle: 99 +wellControls: BHP (at the specified reference elevation): 29829952.030905947 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-01 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 6.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00984824 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222401 s | Solve Time: 0.174004 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.53e-01 ) ; ( Rwell ) = ( 4.65e-07 ) ; ( R ) = ( 8.53e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 2.32e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00977549 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222196 s | Solve Time: 0.172061 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 4.22e-07 ) ; ( R ) = ( 3.35e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00513014 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208281 s | Solve Time: 0.173213 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 9.07e-08 ) ; ( R ) = ( 2.30e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00607408 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205943 s | Solve Time: 0.153033 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00768656 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209885 s | Solve Time: 0.174469 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.133057 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.211168 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 7.22185e+08s, dt:7.38389e+06s, Cycle: 100 +wellControls: BHP (at the specified reference elevation): 29858315.982450448 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-01 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 5.08e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00772353 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227825 s | Solve Time: 0.185089 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.09e-01 ) ; ( Rwell ) = ( 8.01e-07 ) ; ( R ) = ( 7.09e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 4.01e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00755092 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21661 s | Solve Time: 0.172219 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.92e-01 ) ; ( Rwell ) = ( 2.60e-07 ) ; ( R ) = ( 6.92e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 3.26e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0053916 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210026 s | Solve Time: 0.17502 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.88e-02 ) ; ( Rwell ) = ( 7.92e-08 ) ; ( R ) = ( 9.88e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00861491 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215232 s | Solve Time: 0.117913 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 6.56e-08 ) ; ( R ) = ( 8.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.61e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.123071 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.158989 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 7.29569e+08s, dt:7.16909e+06s, Cycle: 101 +wellControls: BHP (at the specified reference elevation): 29881882.913368616 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-01 ) ; ( Rwell ) = ( 6.56e-08 ) ; ( R ) = ( 4.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00513648 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209205 s | Solve Time: 0.177726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.18e-01 ) ; ( Rwell ) = ( 5.62e-07 ) ; ( R ) = ( 8.18e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-01 ) ; ( Rwell ) = ( 2.85e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00435545 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207196 s | Solve Time: 0.177932 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 1.77e-07 ) ; ( R ) = ( 2.41e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00999593 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222845 s | Solve Time: 0.108615 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 1.00e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00497338 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220268 s | Solve Time: 0.133903 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.122104 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.131171 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.36738e+08s, dt:7.64917e+06s, Cycle: 102 +wellControls: BHP (at the specified reference elevation): 29904772.044965204 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 5.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00545328 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224712 s | Solve Time: 0.171874 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-01 ) ; ( Rwell ) = ( 1.67e-07 ) ; ( R ) = ( 5.88e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 8.27e-08 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00597354 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214174 s | Solve Time: 0.174166 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 2.52e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0036331 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21466 s | Solve Time: 0.154538 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 7, 3.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00478386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208042 s | Solve Time: 0.109237 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.129706 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.164291 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 7.44387e+08s, dt:7.30135e+06s, Cycle: 103 +wellControls: BHP (at the specified reference elevation): 29929067.34777364 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-01 ) ; ( Rwell ) = ( 3.85e-09 ) ; ( R ) = ( 4.97e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00434571 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221583 s | Solve Time: 0.173011 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.43e+00 ) ; ( Rwell ) = ( 2.41e-07 ) ; ( R ) = ( 8.43e+00 ) ; + Last LinSolve(iter,res) = ( 8, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e+00 ) ; ( Rwell ) = ( 1.21e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.87e-01 ) ; ( Rwell ) = ( 6.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-01 ) ; ( Rwell ) = ( 3.20e-08 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00429292 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206475 s | Solve Time: 0.173898 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.34e-01 ) ; ( Rwell ) = ( 2.68e-07 ) ; ( R ) = ( 7.34e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-01 ) ; ( Rwell ) = ( 1.50e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00515433 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208742 s | Solve Time: 0.172519 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 6.28e-08 ) ; ( R ) = ( 2.53e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00672095 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210701 s | Solve Time: 0.151309 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.59e-08 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00431654 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209331 s | Solve Time: 0.151752 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.56e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 2.56e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.32e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.113056 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.125514 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.51688e+08s, dt:7.95024e+06s, Cycle: 104 +wellControls: BHP (at the specified reference elevation): 29952488.00000746 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-01 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 5.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00649364 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221729 s | Solve Time: 0.173574 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-01 ) ; ( Rwell ) = ( 3.70e-07 ) ; ( R ) = ( 7.63e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 1.84e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00926913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225774 s | Solve Time: 0.17836 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 6.07e-07 ) ; ( R ) = ( 3.60e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 2.37e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00889644 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216096 s | Solve Time: 0.171674 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00877648 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2107 s | Solve Time: 0.131883 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 7.63e-08 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00638318 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20869 s | Solve Time: 0.156634 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-04 ) ; ( Rwell ) = ( 6.49e-10 ) ; ( R ) = ( 1.53e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.129797 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.13352 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.59638e+08s, dt:8.41235e+06s, Cycle: 105 +wellControls: BHP (at the specified reference elevation): 29977650.63031494 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.49e-01 ) ; ( Rwell ) = ( 6.49e-10 ) ; ( R ) = ( 5.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00519515 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222326 s | Solve Time: 0.215169 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.34e-01 ) ; ( Rwell ) = ( 3.34e-07 ) ; ( R ) = ( 9.34e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-01 ) ; ( Rwell ) = ( 1.67e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00942229 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.231712 s | Solve Time: 0.173127 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 1.78e-06 ) ; ( R ) = ( 3.83e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00531381 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210891 s | Solve Time: 0.156261 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 5.67e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00630649 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214025 s | Solve Time: 0.197752 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.52e-08 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.31e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.12506 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.123408 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.68051e+08s, dt:9.23054e+06s, Cycle: 106 +wellControls: BHP (at the specified reference elevation): 30002972.45722537 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.88e-01 ) ; ( Rwell ) = ( 2.52e-08 ) ; ( R ) = ( 5.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00929982 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207182 s | Solve Time: 0.215812 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-01 ) ; ( Rwell ) = ( 1.01e-06 ) ; ( R ) = ( 5.30e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00883994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227911 s | Solve Time: 0.21535 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 3.26e-07 ) ; ( R ) = ( 2.59e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00727183 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209088 s | Solve Time: 0.2003 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 7.77e-08 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.27e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00592988 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220461 s | Solve Time: 0.216082 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 7.18e-04 ) ; + Last LinSolve(iter,res) = ( 10, 5.93e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.137614 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.135236 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.77281e+08s, dt:9.70831e+06s, Cycle: 107 +wellControls: BHP (at the specified reference elevation): 30031975.594173614 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.97e-01 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 5.97e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00623319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226834 s | Solve Time: 0.23878 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e+00 ) ; ( Rwell ) = ( 5.39e-07 ) ; ( R ) = ( 1.37e+00 ) ; + Last LinSolve(iter,res) = ( 11, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-01 ) ; ( Rwell ) = ( 2.67e-07 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00747291 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207841 s | Solve Time: 0.193408 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 4.07e-07 ) ; ( R ) = ( 3.89e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.47e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00798898 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221396 s | Solve Time: 0.171856 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 1.30e-07 ) ; ( R ) = ( 2.42e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00731316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207877 s | Solve Time: 0.133333 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00802443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207339 s | Solve Time: 0.108815 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; ( R ) = ( 5.78e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.169557 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.147894 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.8699e+08s, dt:1.41046e+06s, Cycle: 108 +wellControls: BHP (at the specified reference elevation): 30062861.978860885 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.56e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; ( R ) = ( 8.56e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00805327 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205137 s | Solve Time: 0.0885332 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.38e-03 ) ; ( Rwell ) = ( 1.13e-06 ) ; ( R ) = ( 8.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0353758 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.025424 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.884e+08s, dt:604800s, Cycle: 109 +wellControls: BHP (at the specified reference elevation): 30067623.656232756 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.27334e+07, 2.9455e+07, 4.11218e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.14151e+06, 3.03251e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45796e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.864e+07, 3.4531e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 3.18219e+10, 3.3551e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00796e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3.18219e+10, 0 }, { 7.217e+09, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 1.13e-06 ) ; ( R ) = ( 3.70e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00778392 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204154 s | Solve Time: 0.0918704 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0247771 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0102136 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89005e+08s, dt:10000s, Cycle: 110 +wellControls: BHP (at the specified reference elevation): 30069669.20311194 Pa +wellControls: Total rate: 49.4855075982387 kg/s; total surface volumetric rate: 26.520417 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52041699999797 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059662926432e-12 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.27355e+07, 2.94571e+07, 4.11238e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.14626e+06, 3.03741e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45796e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.86785e+07, 3.4531e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 3.18486e+10, 3.3551e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00796e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3.18486e+10, 0 }, { 7.22033e+09, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00175317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212653 s | Solve Time: 0.0473138 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.89e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-05 ) ; + Last LinSolve(iter,res) = ( 2, 1.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.144234 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.000168845 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89015e+08s, dt:19856.8s, Cycle: 111 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00733802 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202111 s | Solve Time: 0.062338 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.138506 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.000332754 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89035e+08s, dt:39440.5s, Cycle: 112 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00411774 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215327 s | Solve Time: 0.0839646 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.123641 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.000659511 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89074e+08s, dt:78396.3s, Cycle: 113 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00652435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207371 s | Solve Time: 0.0656684 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.52e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.135721 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.00130498 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89152e+08s, dt:155440s, Cycle: 114 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00793993 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203792 s | Solve Time: 0.10381 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00833345 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206262 s | Solve Time: 0.0937024 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.151141 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.00310549 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89308e+08s, dt:304575s, Cycle: 115 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0043752 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203076 s | Solve Time: 0.124506 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00174578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204738 s | Solve Time: 0.0460798 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-04 ) ; + Last LinSolve(iter,res) = ( 2, 1.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.141454 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.00791266 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.89613e+08s, dt:578626s, Cycle: 116 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0076483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21478 s | Solve Time: 0.104846 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00616953 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230049 s | Solve Time: 0.0659006 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.17e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.151427 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0175945 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.90191e+08s, dt:1.03576e+06s, Cycle: 117 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.53e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00854575 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226342 s | Solve Time: 0.109069 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00495814 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205652 s | Solve Time: 0.0681628 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.144336 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0341959 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.91227e+08s, dt:1.68694e+06s, Cycle: 118 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00880349 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212701 s | Solve Time: 0.104513 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0042152 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219269 s | Solve Time: 0.126096 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.160138 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0556724 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.92914e+08s, dt:2.46063e+06s, Cycle: 119 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00480018 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2088 s | Solve Time: 0.104649 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00630184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213926 s | Solve Time: 0.0669342 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.30e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.131548 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0750332 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.95374e+08s, dt:3.28035e+06s, Cycle: 120 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00464311 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230074 s | Solve Time: 0.109169 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00959211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207239 s | Solve Time: 0.0285317 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.62e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.62e-03 ) ; + Last LinSolve(iter,res) = ( 1, 9.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0853474 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0853374 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.98655e+08s, dt:4.18168e+06s, Cycle: 121 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00970851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206984 s | Solve Time: 0.0910989 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00697101 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206324 s | Solve Time: 0.0692816 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.005409 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208967 s | Solve Time: 0.14585 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.99e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.99e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0561463 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0978316 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.02837e+08s, dt:5.06193e+06s, Cycle: 122 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00784635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218029 s | Solve Time: 0.0879029 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00657864 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22309 s | Solve Time: 0.0857353 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00557686 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20573 s | Solve Time: 0.088176 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00305184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204966 s | Solve Time: 0.0452308 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 2, 3.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0611911 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.103168 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.07898e+08s, dt:5.99829e+06s, Cycle: 123 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00902797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205261 s | Solve Time: 0.0857353 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00401675 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213545 s | Solve Time: 0.111563 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0064699 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205232 s | Solve Time: 0.0473482 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.26e-03 ) ; + Last LinSolve(iter,res) = ( 2, 6.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.063123 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0995418 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.13897e+08s, dt:7.21116e+06s, Cycle: 124 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00982613 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202046 s | Solve Time: 0.0867602 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00780864 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205622 s | Solve Time: 0.106404 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00640296 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202964 s | Solve Time: 0.0847566 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00701764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203187 s | Solve Time: 0.0859146 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0692474 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.14352 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.21108e+08s, dt:7.37037e+06s, Cycle: 125 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00683782 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206877 s | Solve Time: 0.0866302 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e+00 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00448097 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205222 s | Solve Time: 0.107534 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00968737 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205822 s | Solve Time: 0.090745 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00424422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204737 s | Solve Time: 0.126218 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.86e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00754863 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221511 s | Solve Time: 0.106831 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.84e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00774135 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213906 s | Solve Time: 0.0868141 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.37e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0095948 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203371 s | Solve Time: 0.0844424 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.27e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.009435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204643 s | Solve Time: 0.107796 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.04e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00522488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225493 s | Solve Time: 0.12434 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00465336 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205034 s | Solve Time: 0.12583 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0668822 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.129306 +Time: 8.28478e+08s, dt:7.37037e+06s, Cycle: 126 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00705202 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205006 s | Solve Time: 0.0874313 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.45e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00423109 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207395 s | Solve Time: 0.10546 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.42e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00936877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2045 s | Solve Time: 0.0872547 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.44e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00984517 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205774 s | Solve Time: 0.0848937 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.63e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00928325 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20622 s | Solve Time: 0.0858102 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.06e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00941487 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215095 s | Solve Time: 0.086224 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00945194 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210211 s | Solve Time: 0.0936453 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.95e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0094587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209697 s | Solve Time: 0.0887384 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00422602 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209572 s | Solve Time: 0.148414 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0630747 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.144292 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.35849e+08s, dt:7.51332e+06s, Cycle: 127 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00765064 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226777 s | Solve Time: 0.0885132 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.449: ( Rflow ) = ( 5.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.224: ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00943508 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222869 s | Solve Time: 0.0908035 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.47e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0043785 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213154 s | Solve Time: 0.105194 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00608435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204232 s | Solve Time: 0.084871 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00246789 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215739 s | Solve Time: 0.0468962 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.68e-03 ) ; + Last LinSolve(iter,res) = ( 2, 2.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.060496 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.253971 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 8.43362e+08s, dt:5.5796e+06s, Cycle: 128 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00510652 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203182 s | Solve Time: 0.0862984 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00648684 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208464 s | Solve Time: 0.0887662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00331026 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204637 s | Solve Time: 0.0458065 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 2, 3.31e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0428982 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0882398 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.48942e+08s, dt:7.02603e+06s, Cycle: 129 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.008337 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203283 s | Solve Time: 0.0861355 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00618762 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206044 s | Solve Time: 0.0856923 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00722455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204596 s | Solve Time: 0.0851533 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00774071 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211836 s | Solve Time: 0.0451482 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.83e-03 ) ; + Last LinSolve(iter,res) = ( 2, 7.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0509783 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.121092 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.55968e+08s, dt:7.77526e+06s, Cycle: 130 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00747742 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211034 s | Solve Time: 0.0848694 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00652053 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209061 s | Solve Time: 0.0865466 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0096067 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20794 s | Solve Time: 0.0676181 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00568155 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201319 s | Solve Time: 0.0646895 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00927922 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203622 s | Solve Time: 0.12449 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.70e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.70e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.28e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0528994 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.163857 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 8.63743e+08s, dt:7.43198e+06s, Cycle: 131 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00895364 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207053 s | Solve Time: 0.0648552 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00829009 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214587 s | Solve Time: 0.0673934 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00628205 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205913 s | Solve Time: 0.0875508 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0475209 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.126233 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.71175e+08s, dt:8.07144e+06s, Cycle: 132 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00555803 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207914 s | Solve Time: 0.0866933 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00604455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203958 s | Solve Time: 0.0870693 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00615277 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203718 s | Solve Time: 0.0865725 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.47e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00317935 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204408 s | Solve Time: 0.0486927 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 2, 3.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0482282 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.146041 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.79246e+08s, dt:8.17938e+06s, Cycle: 133 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0084852 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20709 s | Solve Time: 0.0929211 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00737733 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205341 s | Solve Time: 0.065109 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.15e-01 ) ; + Last LinSolve(iter,res) = ( 3, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00772297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216157 s | Solve Time: 0.0674643 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.26e-01 ) ; + Last LinSolve(iter,res) = ( 3, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0098505 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211444 s | Solve Time: 0.0698072 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e+00 ) ; + Last LinSolve(iter,res) = ( 3, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00485496 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207165 s | Solve Time: 0.0924667 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.68e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e+00 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0047235 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209149 s | Solve Time: 0.0846647 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00485624 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205802 s | Solve Time: 0.0943453 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00601552 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205613 s | Solve Time: 0.146601 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0456046 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.143889 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8.87426e+08s, dt:8.34944e+06s, Cycle: 134 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00687535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201716 s | Solve Time: 0.0849069 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e+01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e+01 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.435: ( Rflow ) = ( 3.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.218: ( Rflow ) = ( 6.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.109: ( Rflow ) = ( 4.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00780206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203939 s | Solve Time: 0.0855178 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.36e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00451558 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207395 s | Solve Time: 0.106934 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.00e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0065728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216239 s | Solve Time: 0.106 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.02e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00979655 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20422 s | Solve Time: 0.0901838 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.66e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00557818 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204068 s | Solve Time: 0.107769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00579018 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203585 s | Solve Time: 0.085092 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.29e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00679458 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206425 s | Solve Time: 0.0481939 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.30e-02 ) ; + Last LinSolve(iter,res) = ( 2, 6.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00982333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20984 s | Solve Time: 0.128052 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.82e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0433662 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.229127 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 8.95775e+08s, dt:6.60685e+06s, Cycle: 135 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00512171 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209759 s | Solve Time: 0.0875618 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.42e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00735375 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216106 s | Solve Time: 0.0858264 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00386523 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214469 s | Solve Time: 0.0457928 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 2, 3.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00962759 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216656 s | Solve Time: 0.124723 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0324228 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0959399 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.02382e+08s, dt:8.0591e+06s, Cycle: 136 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0084471 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205594 s | Solve Time: 0.0933996 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e+00 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00418919 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204103 s | Solve Time: 0.107919 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00454608 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204701 s | Solve Time: 0.104827 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00828746 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204762 s | Solve Time: 0.125884 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0369077 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132681 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.10441e+08s, dt:8.55285e+06s, Cycle: 137 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.08e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00753486 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218963 s | Solve Time: 0.126766 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.00e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00919117 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219159 s | Solve Time: 0.126196 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00489352 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208021 s | Solve Time: 0.147295 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.005372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206569 s | Solve Time: 0.185 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0363698 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.119658 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.18994e+08s, dt:9.51523e+06s, Cycle: 138 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.63e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00789757 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222156 s | Solve Time: 0.23018 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 11, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0078408 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209548 s | Solve Time: 0.128042 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00674575 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204316 s | Solve Time: 0.126314 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0372142 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.124602 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.28509e+08s, dt:1e+07s, Cycle: 139 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00952714 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221371 s | Solve Time: 0.15061 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00789219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212547 s | Solve Time: 0.210322 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.82e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00459168 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206192 s | Solve Time: 0.187351 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.63e-01 ) ; + Last LinSolve(iter,res) = ( 9, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00565491 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205642 s | Solve Time: 0.187507 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00842915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205674 s | Solve Time: 0.193139 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.83e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.43e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0375822 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.119459 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.38509e+08s, dt:1e+07s, Cycle: 140 +compflowStatistics, reservoir: Pressure (min, average, max): 2.2789e+07, 2.94145e+07, 4.14239e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.4549e+06, 2.71394e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45795e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.76376e+07, 3.45319e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 3.10829e+10, 3.35514e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00794e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3.10829e+10, 0 }, { 8.01775e+09, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00686178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205588 s | Solve Time: 0.190399 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00857235 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206393 s | Solve Time: 0.126838 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00823906 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204288 s | Solve Time: 0.149295 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00814847 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205978 s | Solve Time: 0.10751 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0404615 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.122432 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.48509e+08s, dt:1e+07s, Cycle: 141 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00996813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208751 s | Solve Time: 0.107429 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.22e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00946518 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204543 s | Solve Time: 0.126692 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.26e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00572762 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216909 s | Solve Time: 0.169382 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00570154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207852 s | Solve Time: 0.167917 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00740208 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206334 s | Solve Time: 0.124706 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00611618 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205052 s | Solve Time: 0.186627 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.21e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0407266 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132473 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.58509e+08s, dt:1e+07s, Cycle: 142 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.23e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00943728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205856 s | Solve Time: 0.107177 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e+00 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00802483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204226 s | Solve Time: 0.125299 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e+00 ) ; + Last LinSolve(iter,res) = ( 6, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00561156 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214625 s | Solve Time: 0.125647 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0085969 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20679 s | Solve Time: 0.10726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00628973 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204216 s | Solve Time: 0.185849 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.29e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0394145 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.160118 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 9.68509e+08s, dt:9.67372e+06s, Cycle: 143 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00803309 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21018 s | Solve Time: 0.110051 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00697466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205123 s | Solve Time: 0.11022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00671637 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20776 s | Solve Time: 0.0653791 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00934214 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204076 s | Solve Time: 0.106681 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.69e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0346475 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.101841 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.78183e+08s, dt:1e+07s, Cycle: 144 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00572172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206848 s | Solve Time: 0.112875 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0044599 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207493 s | Solve Time: 0.0930953 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00817987 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207831 s | Solve Time: 0.13444 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.47e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0285615 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102743 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.88183e+08s, dt:1e+07s, Cycle: 145 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00891717 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205735 s | Solve Time: 0.0869948 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00699463 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209089 s | Solve Time: 0.04827 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.68e-02 ) ; + Last LinSolve(iter,res) = ( 2, 6.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.009201 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207218 s | Solve Time: 0.087121 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0295268 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0922109 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 9.98183e+08s, dt:1e+07s, Cycle: 146 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00960686 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21628 s | Solve Time: 0.0887246 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00554858 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207193 s | Solve Time: 0.147668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00786436 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204304 s | Solve Time: 0.0856892 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00859956 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204688 s | Solve Time: 0.0912223 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0302035 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0917369 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.00818e+09s, dt:1e+07s, Cycle: 147 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00677953 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217633 s | Solve Time: 0.105055 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00586646 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205874 s | Solve Time: 0.0706432 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.97e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00748071 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204658 s | Solve Time: 0.107788 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0333422 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0928976 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.01818e+09s, dt:1e+07s, Cycle: 148 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00971888 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204049 s | Solve Time: 0.0943856 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00838178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205698 s | Solve Time: 0.0724954 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00808443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20715 s | Solve Time: 0.155116 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.08e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.032632 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.106052 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.02818e+09s, dt:1e+07s, Cycle: 149 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00600188 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208049 s | Solve Time: 0.117968 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.47e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00919927 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205258 s | Solve Time: 0.110562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00843583 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204257 s | Solve Time: 0.226654 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00937635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206419 s | Solve Time: 0.229831 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.08e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0309805 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.116751 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.03818e+09s, dt:1e+07s, Cycle: 150 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.0090816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203598 s | Solve Time: 0.252299 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.72e-01 ) ; + Last LinSolve(iter,res) = ( 11, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00996731 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205732 s | Solve Time: 0.116726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00761902 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21634 s | Solve Time: 0.0880828 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00989737 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203565 s | Solve Time: 0.148866 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0243619 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.120289 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.04818e+09s, dt:1e+07s, Cycle: 151 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00633015 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203619 s | Solve Time: 0.107925 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.62e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00790426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204967 s | Solve Time: 0.106855 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00625381 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203529 s | Solve Time: 0.0657765 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00801833 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205387 s | Solve Time: 0.171689 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.78e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.78e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0283803 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0868281 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.05818e+09s, dt:1e+07s, Cycle: 152 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00760701 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20407 s | Solve Time: 0.106304 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00996667 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204287 s | Solve Time: 0.0880039 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00993191 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205013 s | Solve Time: 0.125575 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.93e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0286755 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0908067 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.06818e+09s, dt:1e+07s, Cycle: 153 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.46e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00825056 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205508 s | Solve Time: 0.107098 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.44e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00872671 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203484 s | Solve Time: 0.125535 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00602976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203628 s | Solve Time: 0.0667066 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0247729 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0798454 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.07818e+09s, dt:1e+07s, Cycle: 154 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00521592 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202817 s | Solve Time: 0.127285 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00820111 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203372 s | Solve Time: 0.0851046 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00845689 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205974 s | Solve Time: 0.14696 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0237028 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0940451 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.08818e+09s, dt:1e+07s, Cycle: 155 +compflowStatistics, reservoir: Pressure (min, average, max): 2.27364e+07, 2.93722e+07, 4.14977e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.49904e+06, 2.66393e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45793e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.66441e+07, 3.45327e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 3.04299e+10, 3.35517e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00792e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3.04299e+10, 0 }, { 8.70506e+09, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0091702 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206577 s | Solve Time: 0.108328 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00841211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208349 s | Solve Time: 0.109186 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00811716 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2038 s | Solve Time: 0.0657529 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0235042 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0776851 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.09818e+09s, dt:1e+07s, Cycle: 156 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00918581 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202533 s | Solve Time: 0.105207 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.66e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00706276 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205169 s | Solve Time: 0.0675183 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00948613 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202391 s | Solve Time: 0.145315 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0215909 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0818837 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.10818e+09s, dt:1e+07s, Cycle: 157 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00619158 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224375 s | Solve Time: 0.107559 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00487321 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204997 s | Solve Time: 0.0914579 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.006017 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205736 s | Solve Time: 0.148216 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.98e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.98e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.021757 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0754467 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.11818e+09s, dt:1e+07s, Cycle: 158 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00692395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211089 s | Solve Time: 0.109909 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00915252 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213161 s | Solve Time: 0.107986 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00732429 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203653 s | Solve Time: 0.0868077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00757656 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21881 s | Solve Time: 0.144968 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.85e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.58e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0191714 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.092396 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.12818e+09s, dt:1e+07s, Cycle: 159 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00868165 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22076 s | Solve Time: 0.112984 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00999754 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205214 s | Solve Time: 0.0679158 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.33e-02 ) ; + Last LinSolve(iter,res) = ( 3, 1.00e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00806193 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202846 s | Solve Time: 0.12565 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.06e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0186409 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.108947 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.13818e+09s, dt:1e+07s, Cycle: 160 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0042918 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208546 s | Solve Time: 0.125916 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00833926 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202161 s | Solve Time: 0.106435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00452998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218815 s | Solve Time: 0.127603 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.53e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0197062 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.111551 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.14818e+09s, dt:1e+07s, Cycle: 161 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00344277 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214268 s | Solve Time: 0.126066 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 3.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00760356 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215488 s | Solve Time: 0.125054 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0064722 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203142 s | Solve Time: 0.0904339 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0184107 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.1215 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.15818e+09s, dt:1e+07s, Cycle: 162 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00669029 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213734 s | Solve Time: 0.127649 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00436112 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215382 s | Solve Time: 0.147812 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e+00 ) ; + Last LinSolve(iter,res) = ( 7, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0044285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202721 s | Solve Time: 0.14581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00780239 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201906 s | Solve Time: 0.106087 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0173697 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0796031 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.16818e+09s, dt:1e+07s, Cycle: 163 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00501568 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213858 s | Solve Time: 0.135075 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00779351 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203811 s | Solve Time: 0.0857188 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0073536 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207593 s | Solve Time: 0.133417 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.35e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0156793 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0679766 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.17818e+09s, dt:1e+07s, Cycle: 164 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.02e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00781808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215532 s | Solve Time: 0.106126 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00700862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204104 s | Solve Time: 0.127687 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0091192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204915 s | Solve Time: 0.130537 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e+00 ) ; + Last LinSolve(iter,res) = ( 6, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00721723 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20707 s | Solve Time: 0.138719 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0079161 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207929 s | Solve Time: 0.117614 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.015712 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0919463 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.18818e+09s, dt:1e+07s, Cycle: 165 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00576939 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217671 s | Solve Time: 0.125682 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00535025 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207995 s | Solve Time: 0.129554 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00934765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206635 s | Solve Time: 0.0864003 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00460585 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218127 s | Solve Time: 0.126433 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.61e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0140314 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.070426 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.19818e+09s, dt:1e+07s, Cycle: 166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.007607 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20697 s | Solve Time: 0.112988 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00581411 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206754 s | Solve Time: 0.11215 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00746077 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205794 s | Solve Time: 0.111193 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 +wellControls: well is shut + ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.61e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0131155 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0687539 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.20818e+09s, dt:1e+07s, Cycle: 167 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.86e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0096503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216178 s | Solve Time: 0.113887 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00464349 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214945 s | Solve Time: 0.134601 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00577384 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227647 s | Solve Time: 0.0871021 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0165332 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.074551 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.21818e+09s, dt:1e+07s, Cycle: 168 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00516248 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214324 s | Solve Time: 0.129312 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00838658 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203667 s | Solve Time: 0.0851501 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00566041 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20387 s | Solve Time: 0.109467 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0147576 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.113314 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.22818e+09s, dt:1e+07s, Cycle: 169 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.97e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00692338 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223759 s | Solve Time: 0.105424 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00616743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205154 s | Solve Time: 0.136457 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00697801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205549 s | Solve Time: 0.0677951 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.42e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.014482 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115365 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.23818e+09s, dt:1e+07s, Cycle: 170 +compflowStatistics, reservoir: Pressure (min, average, max): 2.26956e+07, 2.9335e+07, 4.14984e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.46408e+06, 2.61907e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45792e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.57826e+07, 3.45334e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.98672e+10, 3.35519e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.0079e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.98672e+10, 0 }, { 9.30304e+09, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00517209 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208565 s | Solve Time: 0.126907 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00716675 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203166 s | Solve Time: 0.125467 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00918156 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209749 s | Solve Time: 0.0866275 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0166146 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12647 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.24818e+09s, dt:1e+07s, Cycle: 171 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00676092 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219423 s | Solve Time: 0.128177 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.04e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203601 s | Solve Time: 0.104704 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0067215 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204272 s | Solve Time: 0.107059 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00619035 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21496 s | Solve Time: 0.148828 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.19e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0150901 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.140833 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.25818e+09s, dt:1e+07s, Cycle: 172 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00740502 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201564 s | Solve Time: 0.106527 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00673116 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203886 s | Solve Time: 0.106218 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0065385 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203973 s | Solve Time: 0.0652279 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0143687 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0912595 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.26818e+09s, dt:1e+07s, Cycle: 173 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00897468 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216746 s | Solve Time: 0.107081 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00632529 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203035 s | Solve Time: 0.105935 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00792163 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212133 s | Solve Time: 0.114044 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0136124 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.101594 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.27818e+09s, dt:1e+07s, Cycle: 174 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00890863 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205907 s | Solve Time: 0.117426 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00902884 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206068 s | Solve Time: 0.0663479 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0053614 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203621 s | Solve Time: 0.0952715 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00569213 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20353 s | Solve Time: 0.0652745 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0127047 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.172882 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.28818e+09s, dt:9.29131e+06s, Cycle: 175 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0049252 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219338 s | Solve Time: 0.127549 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00809415 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212837 s | Solve Time: 0.0857856 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00993075 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204613 s | Solve Time: 0.0863138 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00899764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202759 s | Solve Time: 0.108188 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.36e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0138754 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.149122 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.29747e+09s, dt:9.31859e+06s, Cycle: 176 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00678315 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201646 s | Solve Time: 0.117141 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0098276 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203901 s | Solve Time: 0.109139 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00484825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203809 s | Solve Time: 0.116134 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00651402 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206151 s | Solve Time: 0.125603 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.51e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0158674 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.112211 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.30679e+09s, dt:1e+07s, Cycle: 177 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00817486 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201964 s | Solve Time: 0.127386 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.63e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00651697 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202111 s | Solve Time: 0.0852595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00573123 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218867 s | Solve Time: 0.133516 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00858574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203693 s | Solve Time: 0.185562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0237718 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.125723 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.31679e+09s, dt:1e+07s, Cycle: 178 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00663115 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204275 s | Solve Time: 0.129721 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00688634 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203486 s | Solve Time: 0.165498 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0053535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203578 s | Solve Time: 0.106012 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00939185 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203728 s | Solve Time: 0.107198 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.90e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.90e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0164766 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.138702 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.32679e+09s, dt:1e+07s, Cycle: 179 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00527948 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20523 s | Solve Time: 0.106526 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.40e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00622431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214039 s | Solve Time: 0.106079 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00664578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202469 s | Solve Time: 0.125103 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00835798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202732 s | Solve Time: 0.125564 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.94e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.36e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0233055 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115505 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.33679e+09s, dt:1e+07s, Cycle: 180 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00958008 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209798 s | Solve Time: 0.0870341 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.16e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00942549 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212558 s | Solve Time: 0.0657125 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00849189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214138 s | Solve Time: 0.0881707 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0356152 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.130816 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.34679e+09s, dt:1e+07s, Cycle: 181 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00721388 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201481 s | Solve Time: 0.107097 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00881557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206242 s | Solve Time: 0.0857265 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00895181 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204212 s | Solve Time: 0.10622 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0213482 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.134103 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.35679e+09s, dt:1e+07s, Cycle: 182 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00410148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203168 s | Solve Time: 0.105246 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00577995 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202939 s | Solve Time: 0.0907856 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0059118 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202046 s | Solve Time: 0.109344 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0145158 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.120197 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.36679e+09s, dt:1e+07s, Cycle: 183 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00476652 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219083 s | Solve Time: 0.104429 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.72e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00933818 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203383 s | Solve Time: 0.105084 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00877488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205938 s | Solve Time: 0.111006 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00894976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205068 s | Solve Time: 0.087898 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0170343 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.160778 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.37679e+09s, dt:9.65318e+06s, Cycle: 184 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00896176 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205606 s | Solve Time: 0.106938 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.43e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00617058 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203387 s | Solve Time: 0.125442 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00489543 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216731 s | Solve Time: 0.12932 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00874289 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206352 s | Solve Time: 0.0878282 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0121793 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.170616 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.38645e+09s, dt:9.03247e+06s, Cycle: 185 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0075951 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220416 s | Solve Time: 0.10688 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00792735 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205204 s | Solve Time: 0.118607 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00767386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225186 s | Solve Time: 0.106883 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00861355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208305 s | Solve Time: 0.108602 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00848925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20401 s | Solve Time: 0.104817 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00529398 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203155 s | Solve Time: 0.125673 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00937145 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208594 s | Solve Time: 0.066711 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.033698 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133333 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.39548e+09s, dt:9.56382e+06s, Cycle: 186 +compflowStatistics, reservoir: Pressure (min, average, max): 2.26562e+07, 2.92966e+07, 4.14734e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.42248e+06, 2.57274e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45791e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.49079e+07, 3.45342e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.92968e+10, 3.35521e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00789e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.92968e+10, 0 }, { 9.89229e+09, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00730652 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203203 s | Solve Time: 0.12704 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.12e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00503204 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209237 s | Solve Time: 0.127368 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00490497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204845 s | Solve Time: 0.049879 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 2, 4.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00796786 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220418 s | Solve Time: 0.126422 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0146119 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.119634 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.40504e+09s, dt:1e+07s, Cycle: 187 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00794781 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204607 s | Solve Time: 0.105945 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00701303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209976 s | Solve Time: 0.13199 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.55e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00706436 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209138 s | Solve Time: 0.13206 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00882116 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205543 s | Solve Time: 0.0868599 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0163681 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.139935 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.41504e+09s, dt:1e+07s, Cycle: 188 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00715544 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20403 s | Solve Time: 0.127347 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00583328 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202789 s | Solve Time: 0.126903 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00673182 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214755 s | Solve Time: 0.0898009 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00674639 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202915 s | Solve Time: 0.108931 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.017961 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.204916 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.42504e+09s, dt:8.45271e+06s, Cycle: 189 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00471308 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222281 s | Solve Time: 0.106731 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0086705 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207029 s | Solve Time: 0.112542 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.62e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00705441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205436 s | Solve Time: 0.104794 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0094641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213053 s | Solve Time: 0.085715 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012787 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133638 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.43349e+09s, dt:8.94032e+06s, Cycle: 190 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00950686 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205429 s | Solve Time: 0.116702 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00512747 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204303 s | Solve Time: 0.132922 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00593879 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204476 s | Solve Time: 0.127451 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00992693 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208181 s | Solve Time: 0.0699416 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00749078 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203369 s | Solve Time: 0.105298 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0289961 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.169062 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.44244e+09s, dt:8.40619e+06s, Cycle: 191 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00996031 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221489 s | Solve Time: 0.096279 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.29e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00808554 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210219 s | Solve Time: 0.114848 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00659496 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207837 s | Solve Time: 0.107072 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00807126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21054 s | Solve Time: 0.0855546 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00576768 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208538 s | Solve Time: 0.114489 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.25e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0242982 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.186186 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.45084e+09s, dt:7.50138e+06s, Cycle: 192 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00763733 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208234 s | Solve Time: 0.0945005 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00500549 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218826 s | Solve Time: 0.112791 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00917299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227557 s | Solve Time: 0.0889136 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00793949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206378 s | Solve Time: 0.128127 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0183639 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.114192 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.45834e+09s, dt:8.51808e+06s, Cycle: 193 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00989825 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208334 s | Solve Time: 0.0947249 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00831626 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208228 s | Solve Time: 0.116125 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00933386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215847 s | Solve Time: 0.104819 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.33e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0207039 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.122256 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.46686e+09s, dt:9.38613e+06s, Cycle: 194 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00760065 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2026 s | Solve Time: 0.105143 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.70e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00624939 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207057 s | Solve Time: 0.132131 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00626891 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204707 s | Solve Time: 0.126266 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.25e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.25e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00953756 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204019 s | Solve Time: 0.106267 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00486789 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204993 s | Solve Time: 0.0853714 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00474636 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205531 s | Solve Time: 0.0923191 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00779345 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206631 s | Solve Time: 0.126601 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.74e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.74e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0198653 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.214865 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.47625e+09s, dt:7.71747e+06s, Cycle: 195 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00803488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202453 s | Solve Time: 0.0853676 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.44e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00694279 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203178 s | Solve Time: 0.107013 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00783728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20344 s | Solve Time: 0.085386 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00823535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203801 s | Solve Time: 0.107136 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.24e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0152413 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12257 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.48396e+09s, dt:8.4941e+06s, Cycle: 196 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00559932 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205243 s | Solve Time: 0.105769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00874897 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20405 s | Solve Time: 0.105718 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00535082 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20224 s | Solve Time: 0.111782 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0131751 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.11462 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.49246e+09s, dt:9.62976e+06s, Cycle: 197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00822264 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214199 s | Solve Time: 0.109349 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.45e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0098744 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209485 s | Solve Time: 0.106978 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0060844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213088 s | Solve Time: 0.0900613 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00777601 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22589 s | Solve Time: 0.105318 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.49e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.49e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0225374 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.125842 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.50209e+09s, dt:1e+07s, Cycle: 198 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844291 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210849 s | Solve Time: 0.105136 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00443451 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207451 s | Solve Time: 0.16738 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00760279 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205037 s | Solve Time: 0.105771 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00624519 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204419 s | Solve Time: 0.125939 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0156482 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.139675 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.51209e+09s, dt:1e+07s, Cycle: 199 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00925967 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21885 s | Solve Time: 0.148796 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00695008 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20536 s | Solve Time: 0.106456 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00749328 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212879 s | Solve Time: 0.0854762 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0246168 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.201989 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.52209e+09s, dt:8.523e+06s, Cycle: 200 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.21e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0061925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216662 s | Solve Time: 0.145471 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e+00 ) ; + Last LinSolve(iter,res) = ( 7, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00905168 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205591 s | Solve Time: 0.128133 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00859142 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218901 s | Solve Time: 0.105743 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00799799 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204263 s | Solve Time: 0.0712565 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0272788 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.111162 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.53061e+09s, dt:9.79047e+06s, Cycle: 201 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00952264 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214895 s | Solve Time: 0.146104 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00407586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208995 s | Solve Time: 0.263431 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; + Last LinSolve(iter,res) = ( 12, 4.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0049172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205053 s | Solve Time: 0.0657063 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 3, 4.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00668125 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205673 s | Solve Time: 0.209806 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.26e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.01603 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115957 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.5404e+09s, dt:1e+07s, Cycle: 202 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.84e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00750883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201484 s | Solve Time: 0.172587 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.38e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00932992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205387 s | Solve Time: 0.133411 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00504104 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205785 s | Solve Time: 0.133476 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00948391 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204217 s | Solve Time: 0.134994 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00669273 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204255 s | Solve Time: 0.157104 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0212293 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.123557 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.5504e+09s, dt:1e+07s, Cycle: 203 +compflowStatistics, reservoir: Pressure (min, average, max): 2.26202e+07, 2.92608e+07, 4.14408e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.38687e+06, 2.5285e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.4579e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.40952e+07, 3.45349e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.877e+10, 3.35523e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00787e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.877e+10, 0 }, { 1.04344e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.75e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00711725 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206338 s | Solve Time: 0.147807 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00967621 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204082 s | Solve Time: 0.12535 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0076647 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20366 s | Solve Time: 0.124339 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0182998 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.118953 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.5604e+09s, dt:1e+07s, Cycle: 204 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00896065 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216795 s | Solve Time: 0.106035 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.008861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205582 s | Solve Time: 0.1076 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00748662 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201698 s | Solve Time: 0.103966 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00870847 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203166 s | Solve Time: 0.16758 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.71e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0151199 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.134322 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.5704e+09s, dt:7.60778e+06s, Cycle: 205 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00393489 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200316 s | Solve Time: 0.104912 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Last LinSolve(iter,res) = ( 5, 3.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00774014 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214661 s | Solve Time: 0.0931052 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00792327 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20408 s | Solve Time: 0.125232 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0145889 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.110688 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.57801e+09s, dt:8.75503e+06s, Cycle: 206 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00718029 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212218 s | Solve Time: 0.105953 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.13e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00492685 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202895 s | Solve Time: 0.124956 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e+00 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0049973 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203113 s | Solve Time: 0.12518 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00520809 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202055 s | Solve Time: 0.125161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00706543 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203607 s | Solve Time: 0.0868533 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0168739 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.125391 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.58676e+09s, dt:9.53738e+06s, Cycle: 207 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00663438 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227935 s | Solve Time: 0.126003 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.90e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00564127 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203986 s | Solve Time: 0.107136 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00602852 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204026 s | Solve Time: 0.0851521 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00956388 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204136 s | Solve Time: 0.145241 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.56e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0267813 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.122705 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.5963e+09s, dt:1e+07s, Cycle: 208 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00974215 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203405 s | Solve Time: 0.108048 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00815041 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203522 s | Solve Time: 0.148543 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00573527 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213885 s | Solve Time: 0.126596 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0169212 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.10047 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6063e+09s, dt:1e+07s, Cycle: 209 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00943572 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21333 s | Solve Time: 0.146873 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.21e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00567339 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204841 s | Solve Time: 0.187441 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0077002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204692 s | Solve Time: 0.127768 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0162231 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102249 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6163e+09s, dt:1e+07s, Cycle: 210 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00913084 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203736 s | Solve Time: 0.148219 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00780846 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204579 s | Solve Time: 0.145189 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.72e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0098057 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213385 s | Solve Time: 0.126959 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.81e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0218803 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.114049 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6263e+09s, dt:1e+07s, Cycle: 211 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0081002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201983 s | Solve Time: 0.144214 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00824009 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204639 s | Solve Time: 0.107092 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00874828 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20584 s | Solve Time: 0.191207 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0270969 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.11418 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6363e+09s, dt:1e+07s, Cycle: 212 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00716202 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205047 s | Solve Time: 0.165551 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00957404 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202647 s | Solve Time: 0.104808 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00867378 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228872 s | Solve Time: 0.146167 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.67e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0289051 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.135852 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6463e+09s, dt:1e+07s, Cycle: 213 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00817582 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217317 s | Solve Time: 0.169299 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.06e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00988832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20531 s | Solve Time: 0.165965 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00565635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206075 s | Solve Time: 0.167122 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.89e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.66e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0243939 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12104 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6563e+09s, dt:1e+07s, Cycle: 214 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00761445 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207979 s | Solve Time: 0.170091 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0095935 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209153 s | Solve Time: 0.169661 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00848512 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209094 s | Solve Time: 0.130168 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.29e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00618578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214988 s | Solve Time: 0.172115 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00796505 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207517 s | Solve Time: 0.12606 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.05e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0266964 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.14654 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6663e+09s, dt:1e+07s, Cycle: 215 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00812951 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218693 s | Solve Time: 0.166668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00581578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206604 s | Solve Time: 0.228927 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-01 ) ; + Last LinSolve(iter,res) = ( 11, 5.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00976554 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205907 s | Solve Time: 0.0859979 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00969266 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206236 s | Solve Time: 0.0887055 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00898792 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20557 s | Solve Time: 0.127539 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.030168 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.112725 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.6763e+09s, dt:1e+07s, Cycle: 216 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00929286 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216641 s | Solve Time: 0.208498 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00662038 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209964 s | Solve Time: 0.231127 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00534861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204798 s | Solve Time: 0.0469683 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 2, 5.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00591849 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205027 s | Solve Time: 0.205925 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.95e-04 ) ; + Last LinSolve(iter,res) = ( 10, 5.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0376395 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.155928 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.6863e+09s, dt:9.80622e+06s, Cycle: 217 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.04e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00764251 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201393 s | Solve Time: 0.165767 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.45e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00854688 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207304 s | Solve Time: 0.187917 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.18e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00565905 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203562 s | Solve Time: 0.208492 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.74e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00566923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214869 s | Solve Time: 0.207037 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00876681 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204981 s | Solve Time: 0.189795 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0308673 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.135173 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.69611e+09s, dt:1e+07s, Cycle: 218 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00955442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212465 s | Solve Time: 0.186949 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.98e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00979762 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205769 s | Solve Time: 0.145481 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00585415 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214058 s | Solve Time: 0.18643 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 9, 5.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00908154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202941 s | Solve Time: 0.085536 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0090989 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203011 s | Solve Time: 0.125446 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.019442 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.166588 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.70611e+09s, dt:9.47603e+06s, Cycle: 219 +compflowStatistics, reservoir: Pressure (min, average, max): 2.25858e+07, 2.92264e+07, 4.14064e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.36294e+06, 2.48446e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45788e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.33153e+07, 3.45355e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.8266e+10, 3.35525e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00785e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.8266e+10, 0 }, { 1.09492e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00448965 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209624 s | Solve Time: 0.125042 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.31e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00778539 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21303 s | Solve Time: 0.128876 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.24e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0094383 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204569 s | Solve Time: 0.125049 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00826996 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204439 s | Solve Time: 0.125894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.27e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.016883 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.146965 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.71558e+09s, dt:9.57288e+06s, Cycle: 220 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00787989 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203014 s | Solve Time: 0.125078 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00762897 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202902 s | Solve Time: 0.125562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00779291 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203798 s | Solve Time: 0.0854001 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00516815 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2034 s | Solve Time: 0.145344 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.54e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.17e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0183247 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.1147 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.72516e+09s, dt:1e+07s, Cycle: 221 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00924024 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218242 s | Solve Time: 0.166319 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00704395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204571 s | Solve Time: 0.106764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00772616 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205031 s | Solve Time: 0.149909 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00913992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207239 s | Solve Time: 0.165942 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0161834 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133008 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.73516e+09s, dt:1e+07s, Cycle: 222 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00720227 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204423 s | Solve Time: 0.188445 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.64e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00644755 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202677 s | Solve Time: 0.168625 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00688446 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209052 s | Solve Time: 0.16754 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00735281 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205589 s | Solve Time: 0.170057 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.38e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00844976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222552 s | Solve Time: 0.0490799 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00998224 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203204 s | Solve Time: 0.165485 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0226154 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.147065 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.74516e+09s, dt:1e+07s, Cycle: 223 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.72e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00758932 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203274 s | Solve Time: 0.14655 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00848692 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205134 s | Solve Time: 0.168422 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00595006 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207506 s | Solve Time: 0.145615 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00862166 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205404 s | Solve Time: 0.0863934 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00859812 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205416 s | Solve Time: 0.167621 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.10e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.10e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0212113 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.171783 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.75516e+09s, dt:9.32305e+06s, Cycle: 224 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00535853 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202675 s | Solve Time: 0.14581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00702913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205075 s | Solve Time: 0.157793 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00808025 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20253 s | Solve Time: 0.125884 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00476585 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202825 s | Solve Time: 0.106435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.77e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0163022 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.185888 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.76448e+09s, dt:8.32693e+06s, Cycle: 225 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00511685 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213461 s | Solve Time: 0.134604 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.31e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00865832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20426 s | Solve Time: 0.126519 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00602294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205225 s | Solve Time: 0.166666 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00606021 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211424 s | Solve Time: 0.126649 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.06e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0229045 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.163853 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 1.77281e+09s, dt:7.95938e+06s, Cycle: 226 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0059838 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215386 s | Solve Time: 0.130269 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.63e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0061544 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20599 s | Solve Time: 0.125847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0090911 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207922 s | Solve Time: 0.0879347 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00513898 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20219 s | Solve Time: 0.164927 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.41e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.41e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0220266 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.143887 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.78077e+09s, dt:8.12495e+06s, Cycle: 227 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00537197 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204178 s | Solve Time: 0.125843 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00649776 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20312 s | Solve Time: 0.145489 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00446237 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209159 s | Solve Time: 0.156376 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0091582 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218835 s | Solve Time: 0.065153 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00722014 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206484 s | Solve Time: 0.14565 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0297388 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.128595 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.78889e+09s, dt:8.7492e+06s, Cycle: 228 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00743174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204594 s | Solve Time: 0.148428 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00638169 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204641 s | Solve Time: 0.129206 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00949933 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206224 s | Solve Time: 0.145092 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.02e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0085333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203383 s | Solve Time: 0.166302 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.53e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0209519 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.14401 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.79764e+09s, dt:8.92745e+06s, Cycle: 229 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.33e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00632453 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226928 s | Solve Time: 0.147943 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e+00 ) ; + Last LinSolve(iter,res) = ( 7, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00861435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207079 s | Solve Time: 0.214961 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.46e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00674454 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20424 s | Solve Time: 0.185977 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.11e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00454086 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204287 s | Solve Time: 0.198456 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0177702 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.142565 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.80657e+09s, dt:9.15434e+06s, Cycle: 230 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00772097 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203473 s | Solve Time: 0.153409 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00914406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204093 s | Solve Time: 0.151211 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00730934 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207388 s | Solve Time: 0.1453 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00982916 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209598 s | Solve Time: 0.146117 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.53e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0237114 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.123272 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.81572e+09s, dt:1e+07s, Cycle: 231 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.68e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00778221 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219338 s | Solve Time: 0.169778 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00700657 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20309 s | Solve Time: 0.166161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.21e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00759797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206326 s | Solve Time: 0.170372 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0145918 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.141942 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.82572e+09s, dt:1e+07s, Cycle: 232 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00728099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217287 s | Solve Time: 0.147923 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00960768 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213324 s | Solve Time: 0.0853771 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00766792 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211564 s | Solve Time: 0.148411 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00575959 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214974 s | Solve Time: 0.208124 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-04 ) ; + Last LinSolve(iter,res) = ( 10, 5.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0381562 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.119957 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.83572e+09s, dt:1e+07s, Cycle: 233 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00939192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215444 s | Solve Time: 0.128238 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e+00 ) ; + Last LinSolve(iter,res) = ( 6, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00824152 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203549 s | Solve Time: 0.125867 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.58e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00949576 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218879 s | Solve Time: 0.18852 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00722179 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203325 s | Solve Time: 0.208488 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.22e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0157338 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.114529 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.84572e+09s, dt:1e+07s, Cycle: 234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.19e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00864196 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216705 s | Solve Time: 0.187674 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.59e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00659062 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218975 s | Solve Time: 0.210536 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00782296 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209229 s | Solve Time: 0.212598 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00424018 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213508 s | Solve Time: 0.167675 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.63e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.24e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0181557 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.124078 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.85572e+09s, dt:1e+07s, Cycle: 235 +compflowStatistics, reservoir: Pressure (min, average, max): 2.25536e+07, 2.91945e+07, 4.13739e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.34019e+06, 2.45567e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45787e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.25844e+07, 3.45361e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.77941e+10, 3.35527e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00784e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.77941e+10, 0 }, { 1.14289e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00551835 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204404 s | Solve Time: 0.210341 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e+00 ) ; + Last LinSolve(iter,res) = ( 10, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00986146 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212234 s | Solve Time: 0.208649 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e+00 ) ; + Last LinSolve(iter,res) = ( 10, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00958485 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205319 s | Solve Time: 0.207511 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00785816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204867 s | Solve Time: 0.188609 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00954558 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204697 s | Solve Time: 0.208776 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.05e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0185856 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.113615 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.86572e+09s, dt:1e+07s, Cycle: 236 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00784548 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204265 s | Solve Time: 0.208692 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.76e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00604126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205185 s | Solve Time: 0.230901 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00788246 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203044 s | Solve Time: 0.105145 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00818101 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203651 s | Solve Time: 0.206701 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.03e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0145079 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.121169 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.87572e+09s, dt:1e+07s, Cycle: 237 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00720656 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20317 s | Solve Time: 0.209244 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00961088 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20848 s | Solve Time: 0.151452 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00840992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207889 s | Solve Time: 0.189308 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.0079094 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206383 s | Solve Time: 0.250764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-04 ) ; + Last LinSolve(iter,res) = ( 12, 7.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119733 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.108839 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.88572e+09s, dt:1e+07s, Cycle: 238 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00978137 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205615 s | Solve Time: 0.188996 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.56e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00941586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219181 s | Solve Time: 0.146541 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.56e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00649373 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205253 s | Solve Time: 0.187219 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0130653 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0754026 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.89572e+09s, dt:1e+07s, Cycle: 239 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +wellControls: well is shut + ( Rflow ) = ( 4.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00602377 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206269 s | Solve Time: 0.207386 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00776933 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204474 s | Solve Time: 0.104809 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00865487 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205048 s | Solve Time: 0.206655 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0131806 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100115 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.90572e+09s, dt:1e+07s, Cycle: 240 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00956798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216781 s | Solve Time: 0.193847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00681903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206678 s | Solve Time: 0.207285 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00942535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21534 s | Solve Time: 0.204703 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.43e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0160567 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0966072 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.91572e+09s, dt:1e+07s, Cycle: 241 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00820505 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216287 s | Solve Time: 0.231634 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00618242 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216358 s | Solve Time: 0.229165 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.80e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00948938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20574 s | Solve Time: 0.146211 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0183583 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100984 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.92572e+09s, dt:1e+07s, Cycle: 242 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0099108 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204114 s | Solve Time: 0.187769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00621247 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206928 s | Solve Time: 0.206109 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00637441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20325 s | Solve Time: 0.166868 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0165802 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0919774 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.93572e+09s, dt:1e+07s, Cycle: 243 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00917638 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206415 s | Solve Time: 0.186852 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.38e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00874075 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215206 s | Solve Time: 0.190872 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00659452 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206587 s | Solve Time: 0.18802 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00844311 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20476 s | Solve Time: 0.232524 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.68e-04 ) ; + Last LinSolve(iter,res) = ( 11, 8.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0222896 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.13754 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.94572e+09s, dt:1e+07s, Cycle: 244 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00956648 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203028 s | Solve Time: 0.127591 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.17e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0074394 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206622 s | Solve Time: 0.187044 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0084861 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21692 s | Solve Time: 0.188054 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00853437 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204902 s | Solve Time: 0.112286 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.53e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0310169 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.138655 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.95572e+09s, dt:1e+07s, Cycle: 245 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00863352 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225387 s | Solve Time: 0.231023 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.19e+00 ) ; + Last LinSolve(iter,res) = ( 10, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00553771 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212114 s | Solve Time: 0.25503 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.20e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e+00 ) ; + Last LinSolve(iter,res) = ( 11, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00536317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207235 s | Solve Time: 0.253549 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-01 ) ; + Last LinSolve(iter,res) = ( 11, 5.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00804115 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207469 s | Solve Time: 0.0952605 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00714906 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22 s | Solve Time: 0.240715 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.69e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0235165 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.116912 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.96572e+09s, dt:1e+07s, Cycle: 246 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00905743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205092 s | Solve Time: 0.210263 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.26e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00619388 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214238 s | Solve Time: 0.206557 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00870142 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206468 s | Solve Time: 0.188078 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00867476 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206577 s | Solve Time: 0.25022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-04 ) ; + Last LinSolve(iter,res) = ( 12, 8.67e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0185428 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.110403 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.97572e+09s, dt:1e+07s, Cycle: 247 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00797253 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210891 s | Solve Time: 0.147485 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00625915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206766 s | Solve Time: 0.211812 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00936545 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205248 s | Solve Time: 0.187889 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00743751 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204817 s | Solve Time: 0.187639 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0115539 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.101634 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.98572e+09s, dt:1e+07s, Cycle: 248 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00969052 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203956 s | Solve Time: 0.157672 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.73e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00814448 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203842 s | Solve Time: 0.126077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00553578 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205676 s | Solve Time: 0.178315 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.72e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0110718 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0940555 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 1.99572e+09s, dt:1e+07s, Cycle: 249 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00679113 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217913 s | Solve Time: 0.136477 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.005856 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212544 s | Solve Time: 0.148644 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.68e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00884316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204455 s | Solve Time: 0.207456 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00853452 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204471 s | Solve Time: 0.146441 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00560561 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206101 s | Solve Time: 0.187768 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 9, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00876584 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204704 s | Solve Time: 0.209931 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.18e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0111573 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0997677 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.00572e+09s, dt:1e+07s, Cycle: 250 +compflowStatistics, reservoir: Pressure (min, average, max): 2.25254e+07, 2.91665e+07, 4.13429e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.32064e+06, 2.43208e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45786e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.19502e+07, 3.45367e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.73883e+10, 3.35529e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00782e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.73883e+10, 0 }, { 1.18432e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00600546 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204788 s | Solve Time: 0.169334 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00805325 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225921 s | Solve Time: 0.0867464 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.0057272 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213845 s | Solve Time: 0.252632 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 12, 5.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0122346 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0931039 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.01572e+09s, dt:1e+07s, Cycle: 251 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00892096 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21665 s | Solve Time: 0.209636 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00816181 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205614 s | Solve Time: 0.256255 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.51e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00717885 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208651 s | Solve Time: 0.0867736 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0182537 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.119752 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.02572e+09s, dt:1e+07s, Cycle: 252 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00571083 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217023 s | Solve Time: 0.227828 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e+00 ) ; + Last LinSolve(iter,res) = ( 11, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00812901 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207996 s | Solve Time: 0.231695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00833101 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208314 s | Solve Time: 0.250042 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00891132 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204515 s | Solve Time: 0.230875 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0186945 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.129577 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.03572e+09s, dt:1e+07s, Cycle: 253 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00852919 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207774 s | Solve Time: 0.229131 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e+00 ) ; + Last LinSolve(iter,res) = ( 11, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.0048673 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21206 s | Solve Time: 0.294164 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; + Last LinSolve(iter,res) = ( 14, 4.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00868714 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223503 s | Solve Time: 0.16699 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00910349 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206853 s | Solve Time: 0.166996 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.33e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0232682 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.149425 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.04572e+09s, dt:1e+07s, Cycle: 254 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00884114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228366 s | Solve Time: 0.245805 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.78e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00770857 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22048 s | Solve Time: 0.1749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.94e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00611919 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206543 s | Solve Time: 0.166518 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0137834 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.140611 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.05572e+09s, dt:1e+07s, Cycle: 255 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00838024 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205127 s | Solve Time: 0.149996 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00693265 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205543 s | Solve Time: 0.16763 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0056212 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212391 s | Solve Time: 0.169604 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00902738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20852 s | Solve Time: 0.132847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0179683 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.107261 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.06572e+09s, dt:1e+07s, Cycle: 256 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00767707 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208556 s | Solve Time: 0.107771 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00883868 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204617 s | Solve Time: 0.106214 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00688144 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202293 s | Solve Time: 0.14692 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0280146 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.169418 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.07572e+09s, dt:9.39209e+06s, Cycle: 257 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0062634 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202952 s | Solve Time: 0.108239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00843001 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204045 s | Solve Time: 0.106811 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00717718 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20619 s | Solve Time: 0.12868 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00921101 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207839 s | Solve Time: 0.145525 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.21e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0123797 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0800178 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.08511e+09s, dt:1e+07s, Cycle: 258 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00874288 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204737 s | Solve Time: 0.105978 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00987858 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212137 s | Solve Time: 0.114517 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00564878 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205209 s | Solve Time: 0.185362 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.95e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0171406 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.160694 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.09511e+09s, dt:9.6558e+06s, Cycle: 259 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00863726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207337 s | Solve Time: 0.11656 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00525758 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214384 s | Solve Time: 0.12814 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00771315 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212055 s | Solve Time: 0.0874614 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00523445 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205622 s | Solve Time: 0.189183 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0132512 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12376 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.10477e+09s, dt:1e+07s, Cycle: 260 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00575801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217706 s | Solve Time: 0.12714 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00994566 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203856 s | Solve Time: 0.1254 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00815162 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204337 s | Solve Time: 0.126178 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00611978 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216871 s | Solve Time: 0.146087 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0221654 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.13124 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.11477e+09s, dt:1e+07s, Cycle: 261 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00928271 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203823 s | Solve Time: 0.10528 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00785188 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20512 s | Solve Time: 0.132333 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00966264 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204344 s | Solve Time: 0.086252 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00756334 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205544 s | Solve Time: 0.130726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0261264 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0980833 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.12477e+09s, dt:1e+07s, Cycle: 262 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00627118 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203522 s | Solve Time: 0.128398 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.37e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00745812 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20221 s | Solve Time: 0.145987 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00789071 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206336 s | Solve Time: 0.108134 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0165274 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100329 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.13477e+09s, dt:1e+07s, Cycle: 263 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00839341 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219016 s | Solve Time: 0.12845 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0097425 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205286 s | Solve Time: 0.125932 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.32e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00770882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204708 s | Solve Time: 0.148865 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00640551 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20796 s | Solve Time: 0.10751 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0137051 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0901971 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.14477e+09s, dt:1e+07s, Cycle: 264 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00622331 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206585 s | Solve Time: 0.127241 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.71e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00488725 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206671 s | Solve Time: 0.128279 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00662765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203918 s | Solve Time: 0.132507 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00601172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205459 s | Solve Time: 0.167904 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.01e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.010234 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0901154 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.15477e+09s, dt:1e+07s, Cycle: 265 +compflowStatistics, reservoir: Pressure (min, average, max): 2.24981e+07, 2.91393e+07, 4.13142e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.30223e+06, 2.40358e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45785e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.13375e+07, 3.45372e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.69965e+10, 3.35531e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00781e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.69965e+10, 0 }, { 1.22327e+10, 3.3548e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00576252 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21789 s | Solve Time: 0.132781 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00685672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206504 s | Solve Time: 0.15104 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00877596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211011 s | Solve Time: 0.131161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.52e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0106071 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0756847 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.16477e+09s, dt:1e+07s, Cycle: 266 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00752966 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204825 s | Solve Time: 0.167393 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.20e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00990046 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204083 s | Solve Time: 0.173353 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00662553 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204767 s | Solve Time: 0.149257 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00990781 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203251 s | Solve Time: 0.16636 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0146661 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0719604 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.17477e+09s, dt:1e+07s, Cycle: 267 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00764693 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207353 s | Solve Time: 0.146433 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00714456 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206406 s | Solve Time: 0.187345 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0096451 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208866 s | Solve Time: 0.0682884 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0219588 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0805079 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.18477e+09s, dt:1e+07s, Cycle: 268 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00767283 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203356 s | Solve Time: 0.147718 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00925133 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203126 s | Solve Time: 0.14508 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.33e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00575772 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204213 s | Solve Time: 0.166313 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00859629 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203592 s | Solve Time: 0.105529 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0171374 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0871514 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.19477e+09s, dt:1e+07s, Cycle: 269 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.78e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00993093 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203849 s | Solve Time: 0.174299 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.52e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.009765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203632 s | Solve Time: 0.185924 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 9, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00955289 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203933 s | Solve Time: 0.186628 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e+00 ) ; + Last LinSolve(iter,res) = ( 9, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00964801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203741 s | Solve Time: 0.187365 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.86e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00991928 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210109 s | Solve Time: 0.0851552 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.017223 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0963603 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.20477e+09s, dt:1e+07s, Cycle: 270 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00803442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211324 s | Solve Time: 0.188341 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00877206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203333 s | Solve Time: 0.146881 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00787117 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202228 s | Solve Time: 0.165435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.87e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.02029 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0761817 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.21477e+09s, dt:1e+07s, Cycle: 271 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.68e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00871629 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20625 s | Solve Time: 0.167325 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00856484 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21414 s | Solve Time: 0.187759 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00743808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20422 s | Solve Time: 0.186662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0188805 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0944679 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.22477e+09s, dt:1e+07s, Cycle: 272 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.63e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0097902 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204765 s | Solve Time: 0.131369 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00923641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204812 s | Solve Time: 0.146746 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00951405 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204075 s | Solve Time: 0.186653 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0133064 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0807276 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.23477e+09s, dt:1e+07s, Cycle: 273 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00910594 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204993 s | Solve Time: 0.125991 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00666538 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204684 s | Solve Time: 0.168674 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00643678 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211746 s | Solve Time: 0.165841 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0146356 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0753625 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.24477e+09s, dt:1e+07s, Cycle: 274 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00813557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203223 s | Solve Time: 0.134162 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00738708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203578 s | Solve Time: 0.13505 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00971915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203353 s | Solve Time: 0.155147 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.72e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0106538 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0826894 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.25477e+09s, dt:1e+07s, Cycle: 275 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0096134 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206063 s | Solve Time: 0.112841 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.49e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00724589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204705 s | Solve Time: 0.0504309 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 2, 7.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0073406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202888 s | Solve Time: 0.185549 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0175398 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0831945 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.26477e+09s, dt:1e+07s, Cycle: 276 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00938839 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202587 s | Solve Time: 0.107462 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844365 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204135 s | Solve Time: 0.107484 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00505026 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204299 s | Solve Time: 0.125772 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.65e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0353964 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0686025 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.27477e+09s, dt:1e+07s, Cycle: 277 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00718634 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20442 s | Solve Time: 0.107209 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00832774 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204022 s | Solve Time: 0.105696 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0062285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205172 s | Solve Time: 0.130415 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0139758 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0912927 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.28477e+09s, dt:1e+07s, Cycle: 278 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00742423 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210383 s | Solve Time: 0.126645 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0060584 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208404 s | Solve Time: 0.0881849 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00763314 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202803 s | Solve Time: 0.14487 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.00e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0188292 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0911982 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.29477e+09s, dt:1e+07s, Cycle: 279 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0074929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203702 s | Solve Time: 0.134207 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00550728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205095 s | Solve Time: 0.12612 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00563791 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204612 s | Solve Time: 0.145274 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.67e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0156261 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.088122 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.30477e+09s, dt:1e+07s, Cycle: 280 +compflowStatistics, reservoir: Pressure (min, average, max): 2.24729e+07, 2.91141e+07, 4.12868e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.28131e+06, 2.37784e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45785e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.07665e+07, 3.45377e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.66328e+10, 3.35532e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.0078e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.66328e+10, 0 }, { 1.25902e+10, 3.3548e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00767665 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201082 s | Solve Time: 0.146225 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.91e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00600998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202626 s | Solve Time: 0.12503 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00755664 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201583 s | Solve Time: 0.106503 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.56e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.01607 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100544 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.31477e+09s, dt:1e+07s, Cycle: 281 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00687509 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202074 s | Solve Time: 0.125702 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00615493 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203563 s | Solve Time: 0.133307 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00754668 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202198 s | Solve Time: 0.105165 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.42e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0134475 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0897088 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.32477e+09s, dt:1e+07s, Cycle: 282 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.68e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00808737 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202768 s | Solve Time: 0.124475 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844936 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204154 s | Solve Time: 0.106423 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00616534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201411 s | Solve Time: 0.149929 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.17e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0132542 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0799209 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.33477e+09s, dt:1e+07s, Cycle: 283 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00574368 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200875 s | Solve Time: 0.144886 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.93e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00916013 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202299 s | Solve Time: 0.164536 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.20e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00771564 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203371 s | Solve Time: 0.168974 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00522765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20403 s | Solve Time: 0.227963 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 11, 5.23e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00906587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203012 s | Solve Time: 0.164778 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.60e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.07e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0163627 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0913273 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.34477e+09s, dt:1e+07s, Cycle: 284 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00500956 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200994 s | Solve Time: 0.165895 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.33e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00785728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218579 s | Solve Time: 0.166388 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00576136 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204983 s | Solve Time: 0.189884 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0348566 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.137303 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.35477e+09s, dt:1e+07s, Cycle: 285 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.78e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00957878 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204568 s | Solve Time: 0.144667 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.37e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00573689 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213378 s | Solve Time: 0.146805 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00742369 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202766 s | Solve Time: 0.0849994 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0165586 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115887 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.36477e+09s, dt:2.24407e+06s, Cycle: 286 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.14e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00362264 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222791 s | Solve Time: 0.0687597 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.11e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00538851 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.024506 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.36701e+09s, dt:3.85787e+06s, Cycle: 287 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00454153 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201655 s | Solve Time: 0.0865976 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00815392 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20354 s | Solve Time: 0.104568 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0154484 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0359477 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.37087e+09s, dt:6.22411e+06s, Cycle: 288 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00412259 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20505 s | Solve Time: 0.106498 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00979236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201916 s | Solve Time: 0.0865995 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00678701 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202203 s | Solve Time: 0.134633 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.009483 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0681504 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.3771e+09s, dt:8.55939e+06s, Cycle: 289 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00814434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20658 s | Solve Time: 0.127397 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00735851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203136 s | Solve Time: 0.126077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00689608 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205895 s | Solve Time: 0.107367 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.015589 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0746193 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.38566e+09s, dt:1e+07s, Cycle: 290 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00631586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207274 s | Solve Time: 0.146725 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00853599 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20295 s | Solve Time: 0.104821 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00648136 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203306 s | Solve Time: 0.125055 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0162867 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100096 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.39566e+09s, dt:1e+07s, Cycle: 291 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00615385 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205275 s | Solve Time: 0.146931 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00798934 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208856 s | Solve Time: 0.126733 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00923752 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205013 s | Solve Time: 0.106995 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.24e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0256255 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0939683 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.40566e+09s, dt:1e+07s, Cycle: 292 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00823668 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202901 s | Solve Time: 0.144958 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00523413 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205752 s | Solve Time: 0.106729 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0091464 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203813 s | Solve Time: 0.126428 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.15e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0218764 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0986145 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.41566e+09s, dt:1e+07s, Cycle: 293 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00820782 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205434 s | Solve Time: 0.146316 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00560333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209138 s | Solve Time: 0.150164 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00809259 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212145 s | Solve Time: 0.104831 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012175 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0733209 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.42566e+09s, dt:1e+07s, Cycle: 294 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.006849 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202623 s | Solve Time: 0.167948 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.68e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00673912 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202793 s | Solve Time: 0.167419 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00977765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220481 s | Solve Time: 0.0692252 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00952679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219153 s | Solve Time: 0.147728 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00934558 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20467 s | Solve Time: 0.105266 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.40e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0113739 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0804205 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.43566e+09s, dt:1e+07s, Cycle: 295 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00636155 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223761 s | Solve Time: 0.165974 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.60e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00742818 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224627 s | Solve Time: 0.169476 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e+00 ) ; + Last LinSolve(iter,res) = ( 8, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00684319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205173 s | Solve Time: 0.166147 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.06e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00686842 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207811 s | Solve Time: 0.168074 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.08e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00687844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209076 s | Solve Time: 0.168412 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.09e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00674045 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207173 s | Solve Time: 0.166911 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00874594 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203706 s | Solve Time: 0.145652 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.15e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.15e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.75e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0193873 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100954 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.44566e+09s, dt:1e+07s, Cycle: 296 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00978522 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206368 s | Solve Time: 0.146019 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.57e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0066154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202897 s | Solve Time: 0.145724 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00517998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20616 s | Solve Time: 0.126709 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.037847 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.16144 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.45566e+09s, dt:9.63269e+06s, Cycle: 297 +compflowStatistics, reservoir: Pressure (min, average, max): 2.24476e+07, 2.90892e+07, 4.12607e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.25922e+06, 2.35615e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45784e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.01971e+07, 3.45382e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.6269e+10, 3.35533e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00779e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.6269e+10, 0 }, { 1.29484e+10, 3.3548e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00865626 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207566 s | Solve Time: 0.145443 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00841904 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206996 s | Solve Time: 0.12648 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0061336 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20277 s | Solve Time: 0.164897 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0117915 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.151349 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.46529e+09s, dt:9.58956e+06s, Cycle: 298 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.63e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00709197 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206479 s | Solve Time: 0.146999 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205398 s | Solve Time: 0.104874 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00695188 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20542 s | Solve Time: 0.148533 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00979831 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0999106 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.47488e+09s, dt:1e+07s, Cycle: 299 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.67e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00797927 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205725 s | Solve Time: 0.14584 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e+00 ) ; + Last LinSolve(iter,res) = ( 7, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00638823 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202989 s | Solve Time: 0.186446 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00839316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220241 s | Solve Time: 0.168974 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00772458 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227454 s | Solve Time: 0.168658 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.72e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0100287 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.173008 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.48488e+09s, dt:9.2877e+06s, Cycle: 300 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00922524 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202072 s | Solve Time: 0.170855 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.01e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00632782 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21681 s | Solve Time: 0.187466 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.48e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00785285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202011 s | Solve Time: 0.144628 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00970244 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.194041 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.49417e+09s, dt:8.09877e+06s, Cycle: 301 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00420771 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205254 s | Solve Time: 0.145862 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00965883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2054 s | Solve Time: 0.0455129 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 2, 9.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00752232 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226167 s | Solve Time: 0.150841 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.52e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0148764 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102732 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.50226e+09s, dt:9.61347e+06s, Cycle: 302 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.84e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00858996 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225323 s | Solve Time: 0.278512 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-01 ) ; + Last LinSolve(iter,res) = ( 13, 8.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00778411 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20284 s | Solve Time: 0.146548 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.72e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00880323 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207142 s | Solve Time: 0.147959 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.80e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0311271 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102056 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.51188e+09s, dt:1e+07s, Cycle: 303 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0067867 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21087 s | Solve Time: 0.19164 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.30e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0062286 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208216 s | Solve Time: 0.18957 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.23e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00964353 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226426 s | Solve Time: 0.107513 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.64e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0121735 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0783574 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.52188e+09s, dt:1e+07s, Cycle: 304 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.02e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00581021 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201854 s | Solve Time: 0.18596 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-01 ) ; + Last LinSolve(iter,res) = ( 9, 5.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00784204 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207508 s | Solve Time: 0.152529 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00541145 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227062 s | Solve Time: 0.165543 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.62e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.62e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0139449 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.109857 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.53188e+09s, dt:1e+07s, Cycle: 305 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00834252 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220505 s | Solve Time: 0.144666 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.006089 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202798 s | Solve Time: 0.226904 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.26e-02 ) ; + Last LinSolve(iter,res) = ( 11, 6.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00737259 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202622 s | Solve Time: 0.126431 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.78e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.013462 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0938751 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.54188e+09s, dt:1e+07s, Cycle: 306 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00987572 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227223 s | Solve Time: 0.186707 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.36e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00891715 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210219 s | Solve Time: 0.290069 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 14, 8.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00814195 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208378 s | Solve Time: 0.187117 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0214388 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.135386 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.55188e+09s, dt:1e+07s, Cycle: 307 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00670859 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222871 s | Solve Time: 0.227586 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.30e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00875708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214896 s | Solve Time: 0.229402 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.29e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00658244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205752 s | Solve Time: 0.0854171 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00868162 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207264 s | Solve Time: 0.25787 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-04 ) ; + Last LinSolve(iter,res) = ( 12, 8.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0149321 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.158904 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.56188e+09s, dt:9.71174e+06s, Cycle: 308 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.19e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00542197 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201818 s | Solve Time: 0.207278 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e+00 ) ; + Last LinSolve(iter,res) = ( 10, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00419816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222273 s | Solve Time: 0.18259 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00891577 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223062 s | Solve Time: 0.148797 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00787774 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203521 s | Solve Time: 0.106016 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0335718 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.10246 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.57159e+09s, dt:1e+07s, Cycle: 309 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.26e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00644311 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221021 s | Solve Time: 0.166368 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0058395 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204042 s | Solve Time: 0.169322 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.70e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00969073 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.232392 s | Solve Time: 0.108887 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0140017 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.131967 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.58159e+09s, dt:1e+07s, Cycle: 310 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00820735 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220939 s | Solve Time: 0.167118 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.17e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00876319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215111 s | Solve Time: 0.177093 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.76e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00884723 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210095 s | Solve Time: 0.167672 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.49e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00681204 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226889 s | Solve Time: 0.126246 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0104255 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.105641 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.59159e+09s, dt:1e+07s, Cycle: 311 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0087648 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205004 s | Solve Time: 0.162985 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00394295 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.231387 s | Solve Time: 0.147239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.79e-02 ) ; + Last LinSolve(iter,res) = ( 7, 3.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00498615 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205543 s | Solve Time: 0.125114 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0167144 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0762608 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.60159e+09s, dt:1e+07s, Cycle: 312 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00556099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212092 s | Solve Time: 0.149807 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00491603 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224906 s | Solve Time: 0.146972 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00832743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209484 s | Solve Time: 0.165638 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.33e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0115942 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0883662 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.61159e+09s, dt:1e+07s, Cycle: 313 +compflowStatistics, reservoir: Pressure (min, average, max): 2.24239e+07, 2.9066e+07, 4.12352e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.23922e+06, 2.33748e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45783e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.9657e+07, 3.45386e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.59247e+10, 3.35535e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00778e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.59247e+10, 0 }, { 1.32863e+10, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00785676 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.233735 s | Solve Time: 0.168666 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00918269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204415 s | Solve Time: 0.167327 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.90e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00636761 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228429 s | Solve Time: 0.128091 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00773858 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207581 s | Solve Time: 0.147852 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.17e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.17e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012653 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.140909 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.62159e+09s, dt:1e+07s, Cycle: 314 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00923952 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202689 s | Solve Time: 0.147581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.34e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00851896 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20504 s | Solve Time: 0.130546 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00935003 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212677 s | Solve Time: 0.125893 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00778154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204049 s | Solve Time: 0.145726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0239821 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12659 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.63159e+09s, dt:1e+07s, Cycle: 315 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00764734 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205536 s | Solve Time: 0.125139 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00892353 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208212 s | Solve Time: 0.130056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00543419 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204343 s | Solve Time: 0.105333 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0060921 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221741 s | Solve Time: 0.145476 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0373258 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.144601 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.64159e+09s, dt:1e+07s, Cycle: 316 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00841192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209213 s | Solve Time: 0.125607 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.76e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00839269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210441 s | Solve Time: 0.127982 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0094827 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211782 s | Solve Time: 0.124978 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00933563 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206619 s | Solve Time: 0.0872781 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00591029 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205227 s | Solve Time: 0.105779 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0263381 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.151807 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 2.65159e+09s, dt:9.94013e+06s, Cycle: 317 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00899894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218716 s | Solve Time: 0.128847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e+00 ) ; + Last LinSolve(iter,res) = ( 6, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00741445 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218863 s | Solve Time: 0.167013 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00792076 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211567 s | Solve Time: 0.125235 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00736159 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229169 s | Solve Time: 0.126328 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0164681 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.141807 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.66153e+09s, dt:1e+07s, Cycle: 318 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00468522 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210418 s | Solve Time: 0.146351 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00707072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211153 s | Solve Time: 0.146269 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00648813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206194 s | Solve Time: 0.130239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0246437 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.119058 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.67153e+09s, dt:1e+07s, Cycle: 319 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00758815 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21168 s | Solve Time: 0.125575 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.12e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0066072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205894 s | Solve Time: 0.126749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00992998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207658 s | Solve Time: 0.0857363 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00827321 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205925 s | Solve Time: 0.10662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.27e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0207819 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0984373 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.68153e+09s, dt:1e+07s, Cycle: 320 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00741758 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205789 s | Solve Time: 0.1269 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00588514 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206281 s | Solve Time: 0.0854129 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00695567 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205843 s | Solve Time: 0.126106 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.12e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0132219 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.108135 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.69153e+09s, dt:1e+07s, Cycle: 321 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00714737 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206609 s | Solve Time: 0.124932 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00903182 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20658 s | Solve Time: 0.106881 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00904885 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203693 s | Solve Time: 0.124821 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.79e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0300629 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0935353 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.70153e+09s, dt:1e+07s, Cycle: 322 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00610449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205697 s | Solve Time: 0.125211 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.14e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00915243 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220539 s | Solve Time: 0.105794 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00486877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202802 s | Solve Time: 0.145647 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00920017 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205746 s | Solve Time: 0.107352 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.59e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0155792 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0836461 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.71153e+09s, dt:1e+07s, Cycle: 323 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00573691 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202847 s | Solve Time: 0.124759 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00648189 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205149 s | Solve Time: 0.108624 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.0064934 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208546 s | Solve Time: 0.208097 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 10, 6.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0138492 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100497 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.72153e+09s, dt:1e+07s, Cycle: 324 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00949018 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204675 s | Solve Time: 0.250585 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e+00 ) ; + Last LinSolve(iter,res) = ( 12, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00545915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220736 s | Solve Time: 0.272224 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; + Last LinSolve(iter,res) = ( 13, 5.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00612906 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208879 s | Solve Time: 0.147196 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00842972 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212726 s | Solve Time: 0.164909 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.43e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0254895 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0976163 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.73153e+09s, dt:1e+07s, Cycle: 325 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00715843 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205321 s | Solve Time: 0.147283 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00873768 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203983 s | Solve Time: 0.125942 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00899466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204294 s | Solve Time: 0.20658 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.05e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0144487 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0777887 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.74153e+09s, dt:1e+07s, Cycle: 326 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00863888 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204403 s | Solve Time: 0.187367 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00827938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203521 s | Solve Time: 0.126167 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00912516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223966 s | Solve Time: 0.209928 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.06e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0174073 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.117664 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.75153e+09s, dt:1e+07s, Cycle: 327 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00927653 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207663 s | Solve Time: 0.144593 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00674269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205786 s | Solve Time: 0.186843 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.00554784 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205734 s | Solve Time: 0.274195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-04 ) ; + Last LinSolve(iter,res) = ( 13, 5.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0206009 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.091239 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.76153e+09s, dt:1e+07s, Cycle: 328 +compflowStatistics, reservoir: Pressure (min, average, max): 2.2402e+07, 2.90447e+07, 4.12122e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.21991e+06, 2.31508e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45782e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.91542e+07, 3.45391e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.56028e+10, 3.35536e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00777e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.56028e+10, 0 }, { 1.35994e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00632358 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206738 s | Solve Time: 0.251024 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-01 ) ; + Last LinSolve(iter,res) = ( 12, 6.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00747506 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216375 s | Solve Time: 0.133436 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00586596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205042 s | Solve Time: 0.146072 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.47e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.87e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0272442 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0843114 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.77153e+09s, dt:1e+07s, Cycle: 329 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00962266 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201959 s | Solve Time: 0.104855 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00815552 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20441 s | Solve Time: 0.127857 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00609716 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208262 s | Solve Time: 0.167309 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0269747 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0682304 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.78153e+09s, dt:1e+07s, Cycle: 330 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.90e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00563791 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20645 s | Solve Time: 0.124477 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00704693 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207433 s | Solve Time: 0.149429 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00931502 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207008 s | Solve Time: 0.128813 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0128824 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0836095 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.79153e+09s, dt:1e+07s, Cycle: 331 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00482985 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209648 s | Solve Time: 0.125361 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00792225 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204581 s | Solve Time: 0.149123 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00665778 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211356 s | Solve Time: 0.104937 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0151148 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0953932 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.80153e+09s, dt:1e+07s, Cycle: 332 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00568226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20217 s | Solve Time: 0.126036 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00685027 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204782 s | Solve Time: 0.105702 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00622305 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208161 s | Solve Time: 0.1276 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.018703 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0887853 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.81153e+09s, dt:1e+07s, Cycle: 333 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00623626 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220619 s | Solve Time: 0.125684 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00733936 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206733 s | Solve Time: 0.135435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.34e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00711623 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207635 s | Solve Time: 0.148602 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0218359 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0807918 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.82153e+09s, dt:1e+07s, Cycle: 334 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00721767 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217863 s | Solve Time: 0.125742 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00735327 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207503 s | Solve Time: 0.129881 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e+00 ) ; + Last LinSolve(iter,res) = ( 6, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00732472 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206599 s | Solve Time: 0.131975 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00843717 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227855 s | Solve Time: 0.0877333 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00561744 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205754 s | Solve Time: 0.186018 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.64e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.62e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0189147 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0914861 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.83153e+09s, dt:1e+07s, Cycle: 335 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.86e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00822307 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204548 s | Solve Time: 0.126633 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00744404 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20324 s | Solve Time: 0.109894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00473802 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204273 s | Solve Time: 0.147326 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.39e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0303172 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0752196 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.84153e+09s, dt:1e+07s, Cycle: 336 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00697728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2293 s | Solve Time: 0.128285 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00634976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213259 s | Solve Time: 0.0856482 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00936905 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212237 s | Solve Time: 0.144999 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.014368 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0838161 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.85153e+09s, dt:1e+07s, Cycle: 337 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00623886 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214468 s | Solve Time: 0.127098 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00564622 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20518 s | Solve Time: 0.125935 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00939496 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207434 s | Solve Time: 0.14859 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00933857 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206031 s | Solve Time: 0.0852337 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0237316 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0852137 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.86153e+09s, dt:1e+07s, Cycle: 338 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00582731 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203827 s | Solve Time: 0.125876 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00883454 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203832 s | Solve Time: 0.104892 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00676067 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212785 s | Solve Time: 0.125088 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0296557 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.131778 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.87153e+09s, dt:1e+07s, Cycle: 339 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.96e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00686525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205333 s | Solve Time: 0.12775 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.49e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00844625 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204805 s | Solve Time: 0.0656165 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00612915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212731 s | Solve Time: 0.147279 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.36e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0286997 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0906965 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.88153e+09s, dt:1e+07s, Cycle: 340 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00684101 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204829 s | Solve Time: 0.130262 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00891338 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203898 s | Solve Time: 0.0851257 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00541556 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204714 s | Solve Time: 0.148706 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0268324 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0924822 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.89153e+09s, dt:1e+07s, Cycle: 341 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00871304 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21386 s | Solve Time: 0.109489 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00614011 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204426 s | Solve Time: 0.0856587 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00550523 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219464 s | Solve Time: 0.125499 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.17e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0186779 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0858472 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.90153e+09s, dt:1e+07s, Cycle: 342 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00644398 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205523 s | Solve Time: 0.127665 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00621643 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204078 s | Solve Time: 0.124456 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00777665 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203011 s | Solve Time: 0.144156 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0163721 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0797164 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.91153e+09s, dt:1e+07s, Cycle: 343 +compflowStatistics, reservoir: Pressure (min, average, max): 2.23817e+07, 2.90251e+07, 4.11908e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.19994e+06, 2.29853e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45781e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.8688e+07, 3.45395e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.53047e+10, 3.35538e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00776e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.53047e+10, 0 }, { 1.38853e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00547525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21873 s | Solve Time: 0.124518 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00869283 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20588 s | Solve Time: 0.10721 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00670974 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205301 s | Solve Time: 0.131195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00928449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205497 s | Solve Time: 0.149094 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00955184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204256 s | Solve Time: 0.085039 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0134736 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.120825 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.92153e+09s, dt:1e+07s, Cycle: 344 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0043776 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210243 s | Solve Time: 0.124998 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00730753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20266 s | Solve Time: 0.0860811 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00606933 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204026 s | Solve Time: 0.127447 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0106104 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.117384 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.93153e+09s, dt:1e+07s, Cycle: 345 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00562178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215852 s | Solve Time: 0.127782 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00562059 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204058 s | Solve Time: 0.125751 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00604934 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204027 s | Solve Time: 0.0651164 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.0058329 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204219 s | Solve Time: 0.187703 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0216119 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0992539 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.94153e+09s, dt:1e+07s, Cycle: 346 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00862741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203508 s | Solve Time: 0.126209 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00555943 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203705 s | Solve Time: 0.12532 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00562303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204279 s | Solve Time: 0.127219 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.15e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.62e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0282648 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.107011 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.95153e+09s, dt:1e+07s, Cycle: 347 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00596331 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202406 s | Solve Time: 0.124618 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00687016 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204902 s | Solve Time: 0.0858542 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00930457 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204439 s | Solve Time: 0.125809 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00723306 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204971 s | Solve Time: 0.124896 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.98e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.026076 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0882178 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.96153e+09s, dt:1e+07s, Cycle: 348 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00793882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203372 s | Solve Time: 0.127286 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.49e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00640154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204738 s | Solve Time: 0.166113 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00568332 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203257 s | Solve Time: 0.145604 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0151614 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.134364 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.97153e+09s, dt:1e+07s, Cycle: 349 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00652813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208796 s | Solve Time: 0.125843 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00647766 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220997 s | Solve Time: 0.148161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00833251 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208861 s | Solve Time: 0.106362 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00631497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225765 s | Solve Time: 0.129185 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.31e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0214447 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.101227 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.98153e+09s, dt:1e+07s, Cycle: 350 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00552273 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201566 s | Solve Time: 0.123919 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00610054 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207938 s | Solve Time: 0.124862 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00740128 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202064 s | Solve Time: 0.124664 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00807457 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223522 s | Solve Time: 0.106373 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0386088 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0745091 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 2.99153e+09s, dt:1e+07s, Cycle: 351 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00690619 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20355 s | Solve Time: 0.124648 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.55e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00888431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204777 s | Solve Time: 0.104898 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00792305 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212227 s | Solve Time: 0.164628 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.53e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.53e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.017104 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.101388 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.00153e+09s, dt:1e+07s, Cycle: 352 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00559946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204007 s | Solve Time: 0.124137 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.78e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00587283 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209675 s | Solve Time: 0.124912 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00732987 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202565 s | Solve Time: 0.104364 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0280511 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102748 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.01153e+09s, dt:1e+07s, Cycle: 353 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00503464 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202648 s | Solve Time: 0.125685 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00854723 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202542 s | Solve Time: 0.0844705 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00861263 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203949 s | Solve Time: 0.130906 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.61e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012346 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0919348 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.02153e+09s, dt:1e+07s, Cycle: 354 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00573661 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203714 s | Solve Time: 0.125582 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00908138 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211334 s | Solve Time: 0.124727 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00892877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210551 s | Solve Time: 0.127761 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.13e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0124751 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0950649 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.03153e+09s, dt:1e+07s, Cycle: 355 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00489772 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2202 s | Solve Time: 0.12541 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.76e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00519177 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212775 s | Solve Time: 0.127455 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00791215 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223149 s | Solve Time: 0.0673312 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0166885 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0700291 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.04153e+09s, dt:1e+07s, Cycle: 356 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00576022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201905 s | Solve Time: 0.125005 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.38e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00794065 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202815 s | Solve Time: 0.105581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00879074 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202738 s | Solve Time: 0.146715 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0113496 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0841302 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.05153e+09s, dt:1e+07s, Cycle: 357 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00591112 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216626 s | Solve Time: 0.125794 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00845871 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206225 s | Solve Time: 0.0661581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00885201 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206725 s | Solve Time: 0.146754 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.31e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.027018 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0945528 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.06153e+09s, dt:1e+07s, Cycle: 358 +compflowStatistics, reservoir: Pressure (min, average, max): 2.23628e+07, 2.90066e+07, 4.11709e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.18392e+06, 2.28199e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45781e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.8247e+07, 3.45398e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.50219e+10, 3.35539e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00775e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.50219e+10, 0 }, { 1.41549e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00906244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202143 s | Solve Time: 0.104715 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00587203 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202431 s | Solve Time: 0.124218 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.41e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00876789 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202807 s | Solve Time: 0.10456 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.77e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0331273 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0971159 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.07153e+09s, dt:1e+07s, Cycle: 359 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00982625 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215206 s | Solve Time: 0.109239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00692669 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204749 s | Solve Time: 0.12606 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00602758 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204947 s | Solve Time: 0.128302 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0336242 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0727459 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.08153e+09s, dt:1e+07s, Cycle: 360 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0098872 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202319 s | Solve Time: 0.104519 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00789959 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202381 s | Solve Time: 0.112055 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00640348 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204334 s | Solve Time: 0.127148 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0166953 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.105177 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.09153e+09s, dt:1e+07s, Cycle: 361 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00844557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209204 s | Solve Time: 0.108468 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.38e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00569446 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204832 s | Solve Time: 0.126596 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.22e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00640072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203151 s | Solve Time: 0.127071 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0313479 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.140377 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.10153e+09s, dt:1e+07s, Cycle: 362 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0049763 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200655 s | Solve Time: 0.124909 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00566851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201434 s | Solve Time: 0.144668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00608481 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201563 s | Solve Time: 0.105407 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0351914 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0928088 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.11153e+09s, dt:1e+07s, Cycle: 363 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00713124 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201626 s | Solve Time: 0.12617 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.20e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00781883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205348 s | Solve Time: 0.168447 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00574093 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203558 s | Solve Time: 0.165635 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.47e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.74e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119962 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0628074 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.12153e+09s, dt:1e+07s, Cycle: 364 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00713299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201596 s | Solve Time: 0.144352 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00648954 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203527 s | Solve Time: 0.112233 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00812739 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205145 s | Solve Time: 0.125074 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0110882 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0660481 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.13153e+09s, dt:1e+07s, Cycle: 365 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00779236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2056 s | Solve Time: 0.126477 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00613739 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205274 s | Solve Time: 0.166834 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00905489 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202072 s | Solve Time: 0.0868184 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0116671 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.118193 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.14153e+09s, dt:1e+07s, Cycle: 366 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00821234 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201882 s | Solve Time: 0.124588 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00517411 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203389 s | Solve Time: 0.127277 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00569484 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202638 s | Solve Time: 0.0895915 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.03e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0181934 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0972712 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.15153e+09s, dt:4.48937e+06s, Cycle: 367 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0086478 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203086 s | Solve Time: 0.0681019 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00479086 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20438 s | Solve Time: 0.0892016 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0205196 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0645615 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.15602e+09s, dt:6.27704e+06s, Cycle: 368 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00900681 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203088 s | Solve Time: 0.0666942 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00927853 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206074 s | Solve Time: 0.05034 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.49e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.28e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0141738 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.073221 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.1623e+09s, dt:8.43608e+06s, Cycle: 369 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.92e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00672589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20356 s | Solve Time: 0.107501 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00797742 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201929 s | Solve Time: 0.065006 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 3, 7.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00383913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202447 s | Solve Time: 0.104344 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0217005 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.10507 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.17073e+09s, dt:9.92209e+06s, Cycle: 370 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00577684 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204019 s | Solve Time: 0.167169 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.78e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00619745 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20392 s | Solve Time: 0.146901 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.90e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0055651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207428 s | Solve Time: 0.15084 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0087699 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204178 s | Solve Time: 0.127225 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00665615 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207176 s | Solve Time: 0.134523 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0158595 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.165722 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.18065e+09s, dt:9.428e+06s, Cycle: 371 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00563821 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206196 s | Solve Time: 0.147389 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00594879 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20394 s | Solve Time: 0.106525 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00907874 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22963 s | Solve Time: 0.105846 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00651281 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207987 s | Solve Time: 0.0860752 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0281979 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.131612 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.19008e+09s, dt:1e+07s, Cycle: 372 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00621751 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206536 s | Solve Time: 0.105197 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00780185 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205348 s | Solve Time: 0.104773 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00835128 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207553 s | Solve Time: 0.108811 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00927148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20264 s | Solve Time: 0.0874877 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0281582 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133206 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.20008e+09s, dt:1e+07s, Cycle: 373 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00695528 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201796 s | Solve Time: 0.108163 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00568226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204493 s | Solve Time: 0.129302 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00863724 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216312 s | Solve Time: 0.0879703 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0102261 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115095 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.21008e+09s, dt:1e+07s, Cycle: 374 +compflowStatistics, reservoir: Pressure (min, average, max): 2.23448e+07, 2.8989e+07, 4.11524e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.16844e+06, 2.27238e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.4578e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.78259e+07, 3.45402e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.47513e+10, 3.3554e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00774e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.47513e+10, 0 }, { 1.4411e+10, 3.35481e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00698481 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205698 s | Solve Time: 0.106403 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00727808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206701 s | Solve Time: 0.0878578 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00984989 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210265 s | Solve Time: 0.126559 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00902632 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0866738 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.22008e+09s, dt:1e+07s, Cycle: 375 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00896678 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208912 s | Solve Time: 0.115227 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0068959 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209111 s | Solve Time: 0.125816 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00712946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217219 s | Solve Time: 0.104771 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012617 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0962331 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.23008e+09s, dt:1e+07s, Cycle: 376 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00875793 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20293 s | Solve Time: 0.10729 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00829898 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206996 s | Solve Time: 0.0908027 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00769587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208281 s | Solve Time: 0.164028 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.70e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0164988 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0675173 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.24008e+09s, dt:1e+07s, Cycle: 377 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00468442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203591 s | Solve Time: 0.130555 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00836791 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204761 s | Solve Time: 0.106708 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00775795 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204733 s | Solve Time: 0.0860549 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0155464 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0782193 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.25008e+09s, dt:1e+07s, Cycle: 378 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00983102 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213505 s | Solve Time: 0.104547 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00637019 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204262 s | Solve Time: 0.125707 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00668972 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203999 s | Solve Time: 0.105136 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0233568 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0722582 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.26008e+09s, dt:1e+07s, Cycle: 379 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00484906 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206766 s | Solve Time: 0.127202 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00953645 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214548 s | Solve Time: 0.107013 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00949113 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204176 s | Solve Time: 0.0870114 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0125826 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0780578 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.27008e+09s, dt:1e+07s, Cycle: 380 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00513134 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201538 s | Solve Time: 0.125072 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00912817 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205227 s | Solve Time: 0.125958 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00714225 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202401 s | Solve Time: 0.129229 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0104017 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0919001 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.28008e+09s, dt:1e+07s, Cycle: 381 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00531867 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202653 s | Solve Time: 0.126081 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00531733 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204374 s | Solve Time: 0.125879 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00744042 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20388 s | Solve Time: 0.126237 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0103837 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.085896 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.29008e+09s, dt:1e+07s, Cycle: 382 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00527748 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20781 s | Solve Time: 0.128105 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00705644 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204016 s | Solve Time: 0.0861452 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0094474 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208812 s | Solve Time: 0.124948 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.10e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.45e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0123406 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0788229 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.30008e+09s, dt:1e+07s, Cycle: 383 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00781923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202214 s | Solve Time: 0.107077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0086718 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202968 s | Solve Time: 0.0881403 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00741011 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203525 s | Solve Time: 0.126534 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.016615 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0642673 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.31008e+09s, dt:1e+07s, Cycle: 384 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00797278 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202039 s | Solve Time: 0.104329 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00884871 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201371 s | Solve Time: 0.106817 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0237329 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0594819 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.32008e+09s, dt:1e+07s, Cycle: 385 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00516994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203059 s | Solve Time: 0.125454 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00934222 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20143 s | Solve Time: 0.105678 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00696958 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203215 s | Solve Time: 0.105697 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00403322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203839 s | Solve Time: 0.0649913 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00891568 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0690799 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.33008e+09s, dt:1e+07s, Cycle: 386 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00957408 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203345 s | Solve Time: 0.105868 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00736595 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209885 s | Solve Time: 0.0931204 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0074619 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205779 s | Solve Time: 0.151128 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00988323 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0747435 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.34008e+09s, dt:1e+07s, Cycle: 387 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0093218 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200864 s | Solve Time: 0.105894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.67e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0068672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204262 s | Solve Time: 0.106465 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00625862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203549 s | Solve Time: 0.0867891 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00498472 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203349 s | Solve Time: 0.168018 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.86e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0167886 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.073386 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.35008e+09s, dt:1e+07s, Cycle: 388 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00602703 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200796 s | Solve Time: 0.107688 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00669983 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202893 s | Solve Time: 0.105035 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0191501 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0700752 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.36008e+09s, dt:1e+07s, Cycle: 389 +compflowStatistics, reservoir: Pressure (min, average, max): 2.23285e+07, 2.89732e+07, 4.11347e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.15368e+06, 2.26128e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.4578e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.74462e+07, 3.45405e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.45081e+10, 3.35541e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00773e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.45081e+10, 0 }, { 1.46372e+10, 3.35482e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0084096 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205088 s | Solve Time: 0.105389 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.09e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00679379 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20345 s | Solve Time: 0.125819 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.30e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00681288 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204574 s | Solve Time: 0.134864 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.43e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00675048 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202189 s | Solve Time: 0.125247 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.61e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00663618 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.234119 s | Solve Time: 0.1059 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0273218 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0535994 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.37008e+09s, dt:1e+07s, Cycle: 390 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.03e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00567365 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200999 s | Solve Time: 0.1066 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00611727 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200863 s | Solve Time: 0.125585 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119035 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.060015 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.38008e+09s, dt:1e+07s, Cycle: 391 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00578726 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206931 s | Solve Time: 0.106822 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00904211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201217 s | Solve Time: 0.0852293 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00611131 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207047 s | Solve Time: 0.104491 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0140074 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0636735 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.39008e+09s, dt:1e+07s, Cycle: 392 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00978441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200325 s | Solve Time: 0.0850098 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0094294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201111 s | Solve Time: 0.104433 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00357298 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201163 s | Solve Time: 0.106366 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.013732 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0642915 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.40008e+09s, dt:1e+07s, Cycle: 393 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00596842 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21889 s | Solve Time: 0.112206 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00948416 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202568 s | Solve Time: 0.0650179 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00759267 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203963 s | Solve Time: 0.130186 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0244957 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0776513 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.41008e+09s, dt:1e+07s, Cycle: 394 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00558997 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202466 s | Solve Time: 0.110965 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00591616 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202233 s | Solve Time: 0.105368 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.022456 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0713562 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.42008e+09s, dt:1e+07s, Cycle: 395 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00925855 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200214 s | Solve Time: 0.0867428 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.06e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00843722 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201678 s | Solve Time: 0.106886 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00785244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202953 s | Solve Time: 0.0885024 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0248024 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0797409 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.43008e+09s, dt:1e+07s, Cycle: 396 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00994192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201603 s | Solve Time: 0.0944123 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00454208 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202314 s | Solve Time: 0.124888 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00428628 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217668 s | Solve Time: 0.0848591 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0297466 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0753917 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.44008e+09s, dt:1e+07s, Cycle: 397 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00955401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205572 s | Solve Time: 0.0857454 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00669109 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202872 s | Solve Time: 0.104569 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00451224 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211698 s | Solve Time: 0.107989 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0107264 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0641543 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.45008e+09s, dt:1e+07s, Cycle: 398 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0092126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209265 s | Solve Time: 0.0948483 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00564166 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211601 s | Solve Time: 0.108494 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00717501 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207182 s | Solve Time: 0.146033 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0096455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204188 s | Solve Time: 0.104887 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0215431 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0590428 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.46008e+09s, dt:1e+07s, Cycle: 399 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00884183 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201798 s | Solve Time: 0.0851955 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00429614 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203406 s | Solve Time: 0.0869008 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0208069 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0589047 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.47008e+09s, dt:1e+07s, Cycle: 400 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00829414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203436 s | Solve Time: 0.105598 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00728554 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203974 s | Solve Time: 0.110312 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00554414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208144 s | Solve Time: 0.106611 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00766918 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0656338 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.48008e+09s, dt:1e+07s, Cycle: 401 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00965641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218829 s | Solve Time: 0.0904782 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00476592 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206651 s | Solve Time: 0.126133 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00557442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208943 s | Solve Time: 0.0874772 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012006 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0741287 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.49008e+09s, dt:1e+07s, Cycle: 402 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00982829 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225331 s | Solve Time: 0.085387 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00806792 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205397 s | Solve Time: 0.0922021 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00592694 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205845 s | Solve Time: 0.124688 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00846737 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205995 s | Solve Time: 0.0668912 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.26e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00891203 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0815604 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.50008e+09s, dt:1e+07s, Cycle: 403 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00628148 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216141 s | Solve Time: 0.10521 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00502446 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202124 s | Solve Time: 0.126581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00560883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205408 s | Solve Time: 0.0942068 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0175723 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.124583 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.51008e+09s, dt:1e+07s, Cycle: 404 +compflowStatistics, reservoir: Pressure (min, average, max): 2.23152e+07, 2.89601e+07, 4.11193e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.14143e+06, 2.25141e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45779e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.71296e+07, 3.45408e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.43067e+10, 3.35542e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00772e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.43067e+10, 0 }, { 1.48167e+10, 3.35482e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00977851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203433 s | Solve Time: 0.0868812 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00529028 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203814 s | Solve Time: 0.127268 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00588797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201415 s | Solve Time: 0.125737 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00529038 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202353 s | Solve Time: 0.104668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0275407 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145868 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.52008e+09s, dt:1e+07s, Cycle: 405 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00963961 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201005 s | Solve Time: 0.0851393 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.62e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00877322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214742 s | Solve Time: 0.108374 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00453677 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203753 s | Solve Time: 0.12534 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00853988 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221388 s | Solve Time: 0.0872281 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00805185 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204348 s | Solve Time: 0.0872571 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0246647 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.153851 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.53008e+09s, dt:9.87327e+06s, Cycle: 406 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00626386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20768 s | Solve Time: 0.107075 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00788184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229978 s | Solve Time: 0.10581 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00471007 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202367 s | Solve Time: 0.105211 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00763016 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208095 s | Solve Time: 0.106424 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0169602 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12342 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.53996e+09s, dt:1e+07s, Cycle: 407 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00600154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203568 s | Solve Time: 0.105522 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.21e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00951538 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201436 s | Solve Time: 0.10504 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0057325 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201945 s | Solve Time: 0.124607 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00653163 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201 s | Solve Time: 0.12427 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00839621 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218474 s | Solve Time: 0.105113 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0294529 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.151979 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.54996e+09s, dt:9.93447e+06s, Cycle: 408 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00574419 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209515 s | Solve Time: 0.105 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.59e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00670745 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202157 s | Solve Time: 0.106935 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.009173 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203419 s | Solve Time: 0.107496 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00598002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202578 s | Solve Time: 0.12501 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0206419 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12654 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.55989e+09s, dt:1e+07s, Cycle: 409 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00595561 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202357 s | Solve Time: 0.107562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00906709 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201448 s | Solve Time: 0.0850195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00514401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218969 s | Solve Time: 0.125202 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0249824 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0982163 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.56989e+09s, dt:1e+07s, Cycle: 410 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00649074 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2047 s | Solve Time: 0.108413 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00925044 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202435 s | Solve Time: 0.104992 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00491256 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203998 s | Solve Time: 0.127161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00814712 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212282 s | Solve Time: 0.0853235 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0294146 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0959696 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.57989e+09s, dt:1e+07s, Cycle: 411 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00742432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202684 s | Solve Time: 0.105392 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00550824 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202405 s | Solve Time: 0.107176 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00451243 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202368 s | Solve Time: 0.125088 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.51e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00811219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219302 s | Solve Time: 0.0848227 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119923 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.152688 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.58989e+09s, dt:9.91119e+06s, Cycle: 412 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00648703 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203463 s | Solve Time: 0.104916 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.85e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00733047 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201623 s | Solve Time: 0.106664 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0076759 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201795 s | Solve Time: 0.103985 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00605356 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201157 s | Solve Time: 0.104757 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0110393 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.164768 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 3.5998e+09s, dt:9.44617e+06s, Cycle: 413 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00919785 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218759 s | Solve Time: 0.0910638 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00614894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201424 s | Solve Time: 0.104897 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00828382 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203238 s | Solve Time: 0.105226 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00548946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203661 s | Solve Time: 0.107061 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0291005 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145841 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.60925e+09s, dt:9.57895e+06s, Cycle: 414 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00731814 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201696 s | Solve Time: 0.107417 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00813638 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201231 s | Solve Time: 0.106224 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00898157 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203544 s | Solve Time: 0.104576 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00849031 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203034 s | Solve Time: 0.0855662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0163693 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115553 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.61883e+09s, dt:1e+07s, Cycle: 415 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00776422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205102 s | Solve Time: 0.11551 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.84e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00966289 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204938 s | Solve Time: 0.108705 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00431635 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200425 s | Solve Time: 0.124264 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00810405 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202126 s | Solve Time: 0.0852896 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.88e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.013365 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.149225 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.62883e+09s, dt:1e+07s, Cycle: 416 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0078936 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202646 s | Solve Time: 0.119172 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00656058 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204339 s | Solve Time: 0.107137 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00532862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220978 s | Solve Time: 0.112828 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0133946 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0895554 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.63883e+09s, dt:1e+07s, Cycle: 417 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0079548 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220194 s | Solve Time: 0.11197 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.30e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00562432 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206047 s | Solve Time: 0.125313 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00509564 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205199 s | Solve Time: 0.127899 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00579491 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203032 s | Solve Time: 0.104603 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00879594 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0725378 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.64883e+09s, dt:1e+07s, Cycle: 418 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00805421 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206959 s | Solve Time: 0.105976 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00581791 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203419 s | Solve Time: 0.126574 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00782022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203602 s | Solve Time: 0.124797 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00949249 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205285 s | Solve Time: 0.131343 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.49e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00825349 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.127856 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.65883e+09s, dt:1e+07s, Cycle: 419 +compflowStatistics, reservoir: Pressure (min, average, max): 2.2304e+07, 2.89489e+07, 4.1106e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.13093e+06, 2.2421e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45779e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.68573e+07, 3.4541e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.41347e+10, 3.35543e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00772e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.41347e+10, 0 }, { 1.49658e+10, 3.35482e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00556783 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206462 s | Solve Time: 0.136501 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00631299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206469 s | Solve Time: 0.128702 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00932336 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206278 s | Solve Time: 0.12778 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00807278 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206792 s | Solve Time: 0.127294 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00744231 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208156 s | Solve Time: 0.10588 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0202272 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.116905 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.66883e+09s, dt:1e+07s, Cycle: 420 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00731412 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209622 s | Solve Time: 0.140655 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00906205 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202311 s | Solve Time: 0.125016 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00830498 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203899 s | Solve Time: 0.113547 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00590765 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201247 s | Solve Time: 0.124664 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.96e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.91e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0220594 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145842 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.67883e+09s, dt:1e+07s, Cycle: 421 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00971626 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205895 s | Solve Time: 0.125696 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00820178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205558 s | Solve Time: 0.0852086 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00743895 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220464 s | Solve Time: 0.106003 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0296686 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.104448 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.68883e+09s, dt:1e+07s, Cycle: 422 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0057342 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205625 s | Solve Time: 0.124273 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00665156 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20347 s | Solve Time: 0.12531 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00559301 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207179 s | Solve Time: 0.148332 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.30e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0142129 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0949512 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.69883e+09s, dt:1e+07s, Cycle: 423 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00551954 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206157 s | Solve Time: 0.130114 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00595427 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2039 s | Solve Time: 0.125635 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00739289 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2032 s | Solve Time: 0.105319 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0222256 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0743429 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.70883e+09s, dt:1e+07s, Cycle: 424 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00979586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20492 s | Solve Time: 0.104829 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0071918 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202632 s | Solve Time: 0.125975 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00555981 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20179 s | Solve Time: 0.128281 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0067299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203707 s | Solve Time: 0.128044 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00864503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219885 s | Solve Time: 0.0850873 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.69e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00922763 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0790967 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.71883e+09s, dt:1e+07s, Cycle: 425 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00830383 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205978 s | Solve Time: 0.105195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00952292 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202444 s | Solve Time: 0.0939632 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00565655 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204328 s | Solve Time: 0.127198 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00692106 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0783916 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.72883e+09s, dt:1e+07s, Cycle: 426 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00711659 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200889 s | Solve Time: 0.105399 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00680147 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205259 s | Solve Time: 0.106313 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00846911 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213044 s | Solve Time: 0.132057 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00987912 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214266 s | Solve Time: 0.105175 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.72e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0138461 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0980496 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.73883e+09s, dt:1e+07s, Cycle: 427 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00691422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202253 s | Solve Time: 0.106135 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00979069 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202333 s | Solve Time: 0.104965 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00790069 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202122 s | Solve Time: 0.160235 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.011477 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0848766 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.74883e+09s, dt:1e+07s, Cycle: 428 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00728738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201905 s | Solve Time: 0.10862 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00844249 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210317 s | Solve Time: 0.125234 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00473332 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203585 s | Solve Time: 0.115537 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0127321 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115978 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.75883e+09s, dt:1e+07s, Cycle: 429 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00816862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20215 s | Solve Time: 0.105999 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00971297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202671 s | Solve Time: 0.0861255 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00498463 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205325 s | Solve Time: 0.129416 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0208893 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.102582 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.76883e+09s, dt:1e+07s, Cycle: 430 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00853532 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204202 s | Solve Time: 0.10534 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00485428 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202635 s | Solve Time: 0.125915 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00452222 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203962 s | Solve Time: 0.104823 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00868126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202961 s | Solve Time: 0.106509 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.57e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.57e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0190467 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.145682 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.77883e+09s, dt:1e+07s, Cycle: 431 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00874617 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209106 s | Solve Time: 0.106722 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00683285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20498 s | Solve Time: 0.105077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00537741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203637 s | Solve Time: 0.104668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0273453 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0914125 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.78883e+09s, dt:1e+07s, Cycle: 432 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00947204 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200113 s | Solve Time: 0.11326 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.47e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00852794 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200522 s | Solve Time: 0.0860543 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00876952 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202256 s | Solve Time: 0.125939 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0122193 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0787575 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.79883e+09s, dt:1e+07s, Cycle: 433 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00745777 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204068 s | Solve Time: 0.106809 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00651138 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207539 s | Solve Time: 0.0891971 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00839728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205439 s | Solve Time: 0.0915788 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00579245 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202888 s | Solve Time: 0.0853316 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0173367 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0864672 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.80883e+09s, dt:1e+07s, Cycle: 434 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22925e+07, 2.89376e+07, 4.10939e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.11996e+06, 2.23803e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45778e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.65799e+07, 3.45413e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.39582e+10, 3.35544e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00771e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.39582e+10, 0 }, { 1.51206e+10, 3.35482e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00710446 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201694 s | Solve Time: 0.105738 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00732046 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227315 s | Solve Time: 0.093944 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00801585 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20298 s | Solve Time: 0.16213 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.70e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0206027 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0992319 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.81883e+09s, dt:1e+07s, Cycle: 435 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.04e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00700131 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20275 s | Solve Time: 0.111431 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00694816 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204922 s | Solve Time: 0.104648 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00807278 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218491 s | Solve Time: 0.145261 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0113656 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0826596 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.82883e+09s, dt:1e+07s, Cycle: 436 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00701149 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206096 s | Solve Time: 0.115674 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00664203 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210108 s | Solve Time: 0.116815 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00846018 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205448 s | Solve Time: 0.0949811 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0110478 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.10794 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.83883e+09s, dt:1e+07s, Cycle: 437 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00822443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204951 s | Solve Time: 0.108477 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0093482 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20289 s | Solve Time: 0.105745 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00711317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205932 s | Solve Time: 0.0848563 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00429134 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202677 s | Solve Time: 0.145534 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.29e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0171952 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.109432 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.84883e+09s, dt:1e+07s, Cycle: 438 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00662417 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201931 s | Solve Time: 0.104999 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.53e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00849613 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201759 s | Solve Time: 0.106022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00699355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201452 s | Solve Time: 0.0859553 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012928 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.138067 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.85883e+09s, dt:1e+07s, Cycle: 439 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0081355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209409 s | Solve Time: 0.106072 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.63e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00694191 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202132 s | Solve Time: 0.105006 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00637929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207242 s | Solve Time: 0.110288 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0145727 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0820547 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.86883e+09s, dt:1e+07s, Cycle: 440 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00784022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200881 s | Solve Time: 0.105235 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00942504 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217963 s | Solve Time: 0.0663356 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00699961 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202794 s | Solve Time: 0.146346 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.17e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0143665 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0805626 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.87883e+09s, dt:1e+07s, Cycle: 441 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0080941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204766 s | Solve Time: 0.106224 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00791948 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208326 s | Solve Time: 0.0883684 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00497897 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202155 s | Solve Time: 0.0852022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00500114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217918 s | Solve Time: 0.0855209 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0277395 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0660732 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.88883e+09s, dt:1e+07s, Cycle: 442 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.77e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00777834 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20402 s | Solve Time: 0.106616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00823976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209717 s | Solve Time: 0.0652212 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.005435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212428 s | Solve Time: 0.146435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.43e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0222644 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0705914 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.89883e+09s, dt:1e+07s, Cycle: 443 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00775236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201833 s | Solve Time: 0.105156 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00765871 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202986 s | Solve Time: 0.0854799 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00824662 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202531 s | Solve Time: 0.124879 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.76e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.25e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0090645 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0726482 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.90883e+09s, dt:1e+07s, Cycle: 444 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00760333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203541 s | Solve Time: 0.106987 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00631372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201606 s | Solve Time: 0.105506 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00407357 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204509 s | Solve Time: 0.11305 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0107306 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.069741 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.91883e+09s, dt:1e+07s, Cycle: 445 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00692994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201955 s | Solve Time: 0.104556 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00671682 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203097 s | Solve Time: 0.0670462 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00793217 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202309 s | Solve Time: 0.0849834 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00800371 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222889 s | Solve Time: 0.0866118 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.01285 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0727494 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.92883e+09s, dt:1e+07s, Cycle: 446 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00686005 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227673 s | Solve Time: 0.117618 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00513361 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201827 s | Solve Time: 0.0851645 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0158591 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0704126 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.93883e+09s, dt:6.19754e+06s, Cycle: 447 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00777251 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201776 s | Solve Time: 0.0653428 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00454476 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222071 s | Solve Time: 0.126171 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.74e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0156217 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0415907 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.94502e+09s, dt:9.70435e+06s, Cycle: 448 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0055322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212768 s | Solve Time: 0.106497 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00605436 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220881 s | Solve Time: 0.107662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00847631 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202119 s | Solve Time: 0.104701 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00674423 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0613151 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.95473e+09s, dt:1e+07s, Cycle: 449 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00719427 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204698 s | Solve Time: 0.104616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00765521 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202994 s | Solve Time: 0.108457 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00675524 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204438 s | Solve Time: 0.0862356 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0118665 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0600501 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.96473e+09s, dt:1e+07s, Cycle: 450 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22812e+07, 2.89263e+07, 4.10819e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.1094e+06, 2.23101e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45778e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.63075e+07, 3.45415e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.37848e+10, 3.35545e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00771e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.37848e+10, 0 }, { 1.52732e+10, 3.35482e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00604955 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203864 s | Solve Time: 0.105211 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00881107 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202593 s | Solve Time: 0.0860203 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00992422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202348 s | Solve Time: 0.0850565 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0210947 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0522168 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.97473e+09s, dt:1e+07s, Cycle: 451 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00655214 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205526 s | Solve Time: 0.105319 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0090017 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20685 s | Solve Time: 0.0877509 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00959997 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203264 s | Solve Time: 0.124311 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.60e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0115647 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0593528 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.98473e+09s, dt:1e+07s, Cycle: 452 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00614431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212945 s | Solve Time: 0.115705 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00811466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203131 s | Solve Time: 0.0942785 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00882976 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0569508 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 3.99473e+09s, dt:1e+07s, Cycle: 453 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.62e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00773118 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205494 s | Solve Time: 0.114056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00648693 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203129 s | Solve Time: 0.106213 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00565175 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204514 s | Solve Time: 0.124982 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00913311 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0800822 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.00473e+09s, dt:1e+07s, Cycle: 454 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00539619 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202529 s | Solve Time: 0.105984 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0073248 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20424 s | Solve Time: 0.0725662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.69e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0070981 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202101 s | Solve Time: 0.105879 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.42e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00786544 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0897631 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.01473e+09s, dt:1e+07s, Cycle: 455 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00514257 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204845 s | Solve Time: 0.105291 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00639206 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202333 s | Solve Time: 0.127716 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00659214 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205528 s | Solve Time: 0.108562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00596257 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203058 s | Solve Time: 0.0849201 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0121623 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0847812 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.02473e+09s, dt:1e+07s, Cycle: 456 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00577175 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200839 s | Solve Time: 0.106803 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0095294 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202227 s | Solve Time: 0.0851217 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00533797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203189 s | Solve Time: 0.125316 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0148987 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0887621 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.03473e+09s, dt:1e+07s, Cycle: 457 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00980512 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207617 s | Solve Time: 0.0897797 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00986061 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202807 s | Solve Time: 0.110528 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00927794 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211663 s | Solve Time: 0.105442 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0135134 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.076545 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.04473e+09s, dt:1e+07s, Cycle: 458 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00479876 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204342 s | Solve Time: 0.117558 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00853856 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211386 s | Solve Time: 0.0924884 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00900276 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203937 s | Solve Time: 0.117197 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.81e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0254828 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.079621 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.05473e+09s, dt:1e+07s, Cycle: 459 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00537103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213665 s | Solve Time: 0.105405 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00989866 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220123 s | Solve Time: 0.0853353 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00849274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207234 s | Solve Time: 0.0891639 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00506545 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209526 s | Solve Time: 0.125104 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0124166 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.133248 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.06473e+09s, dt:1e+07s, Cycle: 460 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.005298 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207883 s | Solve Time: 0.113775 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00559949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205227 s | Solve Time: 0.11401 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00789813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205961 s | Solve Time: 0.116524 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00903964 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201288 s | Solve Time: 0.0944155 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0121186 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.152309 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.07473e+09s, dt:9.92363e+06s, Cycle: 461 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00988887 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221342 s | Solve Time: 0.0859509 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00455844 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201851 s | Solve Time: 0.10484 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00782039 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20785 s | Solve Time: 0.105277 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.97e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00722874 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.085243 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.08465e+09s, dt:1e+07s, Cycle: 462 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0098532 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219827 s | Solve Time: 0.0947349 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00680256 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202001 s | Solve Time: 0.0872504 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00752186 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204076 s | Solve Time: 0.0863003 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00880312 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.115359 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.09465e+09s, dt:1e+07s, Cycle: 463 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0091204 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2042 s | Solve Time: 0.0862077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00592862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20366 s | Solve Time: 0.105307 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00798167 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204749 s | Solve Time: 0.126769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00931819 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205113 s | Solve Time: 0.10563 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.32e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00945121 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0730022 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.10465e+09s, dt:1e+07s, Cycle: 464 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00988956 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205184 s | Solve Time: 0.0980851 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00488003 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202677 s | Solve Time: 0.0856953 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00831853 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207409 s | Solve Time: 0.113987 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.20e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.32e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00786638 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0879597 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.11465e+09s, dt:1e+07s, Cycle: 465 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22707e+07, 2.89159e+07, 4.10707e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.09919e+06, 2.22302e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45778e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.60558e+07, 3.45417e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.36246e+10, 3.35546e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.0077e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.36246e+10, 0 }, { 1.54164e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0050131 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207945 s | Solve Time: 0.107075 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00786452 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20251 s | Solve Time: 0.0876359 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00681276 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208194 s | Solve Time: 0.124942 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0140048 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.091538 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.12465e+09s, dt:1e+07s, Cycle: 466 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.92e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00938435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205919 s | Solve Time: 0.0941064 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00988994 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218217 s | Solve Time: 0.0745212 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00882226 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210298 s | Solve Time: 0.104548 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.47e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.82e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0126416 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.090756 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.13465e+09s, dt:1e+07s, Cycle: 467 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00983795 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202349 s | Solve Time: 0.0858959 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00589192 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214371 s | Solve Time: 0.107151 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00745709 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206442 s | Solve Time: 0.106769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.46e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0148123 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0830013 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.14465e+09s, dt:1e+07s, Cycle: 468 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0057165 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208891 s | Solve Time: 0.118137 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00675063 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210116 s | Solve Time: 0.116382 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00810515 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208791 s | Solve Time: 0.09678 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00559873 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208372 s | Solve Time: 0.0852005 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0236758 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.095545 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.15465e+09s, dt:1e+07s, Cycle: 469 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00991465 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200542 s | Solve Time: 0.0853668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00724597 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216886 s | Solve Time: 0.085822 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00809621 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2056 s | Solve Time: 0.109553 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.20e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0173277 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0834493 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.16465e+09s, dt:1e+07s, Cycle: 470 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00981671 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202113 s | Solve Time: 0.0948952 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00411858 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207818 s | Solve Time: 0.0968981 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00770668 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203247 s | Solve Time: 0.116444 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.39e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.71e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0121769 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0760889 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.17465e+09s, dt:1e+07s, Cycle: 471 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00630758 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215323 s | Solve Time: 0.10499 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00601957 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20656 s | Solve Time: 0.112104 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00592338 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204116 s | Solve Time: 0.105656 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00633731 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201338 s | Solve Time: 0.0853461 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.015275 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0695502 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.18465e+09s, dt:1e+07s, Cycle: 472 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.77e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00663152 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213069 s | Solve Time: 0.116406 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00633103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201509 s | Solve Time: 0.0861293 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0089483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201451 s | Solve Time: 0.124869 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.30e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0088464 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0594228 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.19465e+09s, dt:1e+07s, Cycle: 473 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.68e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00589024 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202605 s | Solve Time: 0.104902 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00621485 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205045 s | Solve Time: 0.0862147 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0055502 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21008 s | Solve Time: 0.104987 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00869331 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0694845 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.20465e+09s, dt:1e+07s, Cycle: 474 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00910527 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201552 s | Solve Time: 0.0865491 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00856792 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202315 s | Solve Time: 0.0854739 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00652525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203683 s | Solve Time: 0.0880186 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0063004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211957 s | Solve Time: 0.0898926 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0115951 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.103766 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.21465e+09s, dt:1e+07s, Cycle: 475 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00567684 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203852 s | Solve Time: 0.106735 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00683598 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202585 s | Solve Time: 0.0881707 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00874305 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202442 s | Solve Time: 0.0867993 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0101686 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0909338 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.22465e+09s, dt:1e+07s, Cycle: 476 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.59e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00956764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200536 s | Solve Time: 0.0850595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0072371 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203535 s | Solve Time: 0.10591 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00695544 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214034 s | Solve Time: 0.107066 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.53e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.53e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0129585 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0606625 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.23465e+09s, dt:1e+07s, Cycle: 477 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00784128 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202122 s | Solve Time: 0.0850493 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00699659 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204502 s | Solve Time: 0.105866 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00904252 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203038 s | Solve Time: 0.104675 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0169351 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.106489 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.24465e+09s, dt:1e+07s, Cycle: 478 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00486305 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202374 s | Solve Time: 0.110056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.28e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00975143 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20334 s | Solve Time: 0.0452866 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 2, 9.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00522462 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203606 s | Solve Time: 0.128749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0135482 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0857992 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.25465e+09s, dt:1e+07s, Cycle: 479 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00547574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202429 s | Solve Time: 0.105331 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00943484 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206042 s | Solve Time: 0.0873563 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0114755 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0731794 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.26465e+09s, dt:1e+07s, Cycle: 480 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22604e+07, 2.89058e+07, 4.10602e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.08758e+06, 2.21288e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45777e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.5815e+07, 3.45419e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.3471e+10, 3.35546e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.0077e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.3471e+10, 0 }, { 1.55553e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0061764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202017 s | Solve Time: 0.105623 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00837355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203546 s | Solve Time: 0.109265 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00800728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203057 s | Solve Time: 0.105703 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.01e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0156042 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0760094 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.27465e+09s, dt:1e+07s, Cycle: 481 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00374416 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204897 s | Solve Time: 0.127454 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.14e-01 ) ; + Last LinSolve(iter,res) = ( 6, 3.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00776613 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206421 s | Solve Time: 0.106349 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00667506 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204957 s | Solve Time: 0.0655845 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0123161 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0768024 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.28465e+09s, dt:1e+07s, Cycle: 482 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00420964 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211364 s | Solve Time: 0.127283 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00384968 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206096 s | Solve Time: 0.126785 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00861258 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203897 s | Solve Time: 0.110791 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.61e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00824024 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0788042 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.29465e+09s, dt:1e+07s, Cycle: 483 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0064568 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206175 s | Solve Time: 0.108974 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00545516 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204368 s | Solve Time: 0.0855621 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00444741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203937 s | Solve Time: 0.085249 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119097 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132973 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.30465e+09s, dt:1e+07s, Cycle: 484 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00805472 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204191 s | Solve Time: 0.106349 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00418114 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202697 s | Solve Time: 0.0868807 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00628603 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205938 s | Solve Time: 0.0870712 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00737755 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203459 s | Solve Time: 0.105427 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0107213 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0886967 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.31465e+09s, dt:1e+07s, Cycle: 485 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00510532 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202313 s | Solve Time: 0.104972 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00886602 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204134 s | Solve Time: 0.104796 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00578659 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201542 s | Solve Time: 0.10434 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0117416 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.112584 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.32465e+09s, dt:1e+07s, Cycle: 486 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00980401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201359 s | Solve Time: 0.104557 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00962497 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202358 s | Solve Time: 0.106083 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00571688 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201994 s | Solve Time: 0.087711 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.23e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00967641 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.100161 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.33465e+09s, dt:1e+07s, Cycle: 487 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00941004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222857 s | Solve Time: 0.105162 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00428496 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202658 s | Solve Time: 0.105837 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00459302 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204061 s | Solve Time: 0.087503 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0103431 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.11618 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.34465e+09s, dt:1e+07s, Cycle: 488 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00715007 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211472 s | Solve Time: 0.111042 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00704133 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203937 s | Solve Time: 0.107207 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00860052 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204435 s | Solve Time: 0.0650595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00334103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206422 s | Solve Time: 0.0852599 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.26e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0115914 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0797265 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.35465e+09s, dt:1e+07s, Cycle: 489 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00484559 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201674 s | Solve Time: 0.104771 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00866641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203297 s | Solve Time: 0.046509 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00766287 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201174 s | Solve Time: 0.124694 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.27e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0117675 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0993808 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.36465e+09s, dt:1e+07s, Cycle: 490 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00425372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200364 s | Solve Time: 0.104737 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00796297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203037 s | Solve Time: 0.0859601 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00569146 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204543 s | Solve Time: 0.0679782 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0174655 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.132795 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.37465e+09s, dt:1e+07s, Cycle: 491 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0074449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22254 s | Solve Time: 0.105586 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00688366 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20127 s | Solve Time: 0.104673 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00749705 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20274 s | Solve Time: 0.0861513 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0229294 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0976421 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.38465e+09s, dt:1e+07s, Cycle: 492 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00815242 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201686 s | Solve Time: 0.105289 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00753105 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206925 s | Solve Time: 0.0867618 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00484679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204214 s | Solve Time: 0.107146 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0144207 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.130706 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.39465e+09s, dt:1e+07s, Cycle: 493 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00635821 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228111 s | Solve Time: 0.107702 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00569163 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204305 s | Solve Time: 0.127061 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0150826 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0867479 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.40465e+09s, dt:1e+07s, Cycle: 494 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00918964 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200351 s | Solve Time: 0.0855417 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00561204 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201386 s | Solve Time: 0.124794 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00609559 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201675 s | Solve Time: 0.0855082 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.32e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0103277 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0784561 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.41465e+09s, dt:1e+07s, Cycle: 495 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22493e+07, 2.8895e+07, 4.10496e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.07777e+06, 2.20127e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45777e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.55629e+07, 3.45421e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.33091e+10, 3.35547e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00769e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.33091e+10, 0 }, { 1.57049e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00929982 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219241 s | Solve Time: 0.0914736 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0093915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205344 s | Solve Time: 0.11114 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.98e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00880744 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206991 s | Solve Time: 0.0922895 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00538696 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208072 s | Solve Time: 0.105201 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0101804 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.12753 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.42465e+09s, dt:1e+07s, Cycle: 496 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00842396 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215275 s | Solve Time: 0.0869714 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00682813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202046 s | Solve Time: 0.104796 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.47e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00713238 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209822 s | Solve Time: 0.105482 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00983605 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20478 s | Solve Time: 0.0455643 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.40e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0136495 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.199514 +compositionalMultiphaseReservoirSolver: Time-step required will be decreased based on state change. +Time: 4.43465e+09s, dt:8.58336e+06s, Cycle: 497 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0059725 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220268 s | Solve Time: 0.105668 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00821483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204708 s | Solve Time: 0.104821 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0097781 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207526 s | Solve Time: 0.105493 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0148745 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.11436 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.44324e+09s, dt:9.74053e+06s, Cycle: 498 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00567227 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202708 s | Solve Time: 0.104939 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00835385 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201233 s | Solve Time: 0.106139 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00963727 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202321 s | Solve Time: 0.105869 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.80e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0060703 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0676248 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.45298e+09s, dt:1e+07s, Cycle: 499 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0098913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218309 s | Solve Time: 0.0854684 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00850955 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208975 s | Solve Time: 0.107696 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00957955 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0509187 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.46298e+09s, dt:1e+07s, Cycle: 500 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00717576 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215078 s | Solve Time: 0.105221 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00596813 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201765 s | Solve Time: 0.124806 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0107176 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0497381 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.47298e+09s, dt:1e+07s, Cycle: 501 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00552944 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222998 s | Solve Time: 0.105961 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00620899 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223045 s | Solve Time: 0.104965 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00646099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208749 s | Solve Time: 0.106705 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0113872 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0508388 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.48298e+09s, dt:1e+07s, Cycle: 502 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00490346 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207744 s | Solve Time: 0.105731 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00664151 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206374 s | Solve Time: 0.124808 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00797472 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207444 s | Solve Time: 0.0879313 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.32e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0133632 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0525553 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.49298e+09s, dt:1e+07s, Cycle: 503 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00661583 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221708 s | Solve Time: 0.107379 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00724923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202139 s | Solve Time: 0.105162 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00653998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203798 s | Solve Time: 0.105236 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0109578 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0498468 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.50298e+09s, dt:1e+07s, Cycle: 504 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00867254 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217376 s | Solve Time: 0.0892447 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00867466 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205191 s | Solve Time: 0.0855671 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0143922 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0534237 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.51298e+09s, dt:1e+07s, Cycle: 505 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0063488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222385 s | Solve Time: 0.10921 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00500601 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20721 s | Solve Time: 0.0848286 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0129333 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0540034 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.52298e+09s, dt:1e+07s, Cycle: 506 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00760255 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204659 s | Solve Time: 0.087056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.007069 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202765 s | Solve Time: 0.10717 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00912093 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206668 s | Solve Time: 0.104836 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.013192 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0779045 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.53298e+09s, dt:1e+07s, Cycle: 507 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00754488 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228192 s | Solve Time: 0.0874974 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0063306 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201754 s | Solve Time: 0.105032 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00673051 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203279 s | Solve Time: 0.105834 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0133407 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.089528 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.54298e+09s, dt:1e+07s, Cycle: 508 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00809972 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221974 s | Solve Time: 0.0865391 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00966933 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206803 s | Solve Time: 0.10818 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.67e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0120987 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0668684 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.55298e+09s, dt:1e+07s, Cycle: 509 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0081679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215851 s | Solve Time: 0.0873091 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00557762 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206317 s | Solve Time: 0.106826 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00451965 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21742 s | Solve Time: 0.104797 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.52e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00984366 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0678065 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.56298e+09s, dt:1e+07s, Cycle: 510 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22413e+07, 2.88869e+07, 4.10399e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.07087e+06, 2.19286e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45777e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.53707e+07, 3.45423e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.31878e+10, 3.35548e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00769e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.31878e+10, 0 }, { 1.58168e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00923107 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201493 s | Solve Time: 0.0856611 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00979767 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204719 s | Solve Time: 0.088836 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00476764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207552 s | Solve Time: 0.127357 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119164 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0925898 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.57298e+09s, dt:1e+07s, Cycle: 511 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00870619 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203692 s | Solve Time: 0.0852107 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00886144 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201604 s | Solve Time: 0.104688 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.61e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.86e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00841526 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0739446 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.58298e+09s, dt:1e+07s, Cycle: 512 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0088343 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217715 s | Solve Time: 0.0866139 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00644299 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201878 s | Solve Time: 0.125079 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.67e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0114385 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0603857 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.59298e+09s, dt:1e+07s, Cycle: 513 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00705235 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221205 s | Solve Time: 0.0879215 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00897022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202571 s | Solve Time: 0.0857627 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00902776 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211435 s | Solve Time: 0.126264 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.012521 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0557529 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.60298e+09s, dt:1e+07s, Cycle: 514 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00661435 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20111 s | Solve Time: 0.0851046 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00772645 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222291 s | Solve Time: 0.0872086 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00581212 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202364 s | Solve Time: 0.104639 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00740574 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0674541 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.61298e+09s, dt:1e+07s, Cycle: 515 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00595988 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220562 s | Solve Time: 0.0874944 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00998161 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206597 s | Solve Time: 0.104676 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00812571 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208948 s | Solve Time: 0.111617 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0114516 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.067062 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.62298e+09s, dt:1e+07s, Cycle: 516 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00765252 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.226606 s | Solve Time: 0.0879133 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0060324 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222954 s | Solve Time: 0.126273 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00673184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209202 s | Solve Time: 0.108057 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0166837 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0675392 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.63298e+09s, dt:1e+07s, Cycle: 517 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00643178 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222364 s | Solve Time: 0.0881267 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00583372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207127 s | Solve Time: 0.105138 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.85e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00673332 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204015 s | Solve Time: 0.125229 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00526885 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204307 s | Solve Time: 0.124943 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.42e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.27e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0177193 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0665597 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.64298e+09s, dt:1e+07s, Cycle: 518 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00824929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206303 s | Solve Time: 0.10746 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00470441 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219116 s | Solve Time: 0.104883 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00487073 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203356 s | Solve Time: 0.0882627 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.017725 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0583206 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.65298e+09s, dt:1e+07s, Cycle: 519 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00761495 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204712 s | Solve Time: 0.0854639 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00911346 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206015 s | Solve Time: 0.086527 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0169379 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0486628 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.66298e+09s, dt:1e+07s, Cycle: 520 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00590612 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200321 s | Solve Time: 0.0862402 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.29e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00551982 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208852 s | Solve Time: 0.106925 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00738971 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.229492 s | Solve Time: 0.0871171 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0159765 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0802586 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.67298e+09s, dt:1e+07s, Cycle: 521 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00701045 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221354 s | Solve Time: 0.0857078 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00787992 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218984 s | Solve Time: 0.105277 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0105351 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.128745 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.68298e+09s, dt:1e+07s, Cycle: 522 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.29e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00854512 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216645 s | Solve Time: 0.0864699 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.97e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00717287 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219585 s | Solve Time: 0.104738 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00858227 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215659 s | Solve Time: 0.107622 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119636 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0882382 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.69298e+09s, dt:1e+07s, Cycle: 523 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.29e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0060078 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205288 s | Solve Time: 0.0858177 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.56e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00609499 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22069 s | Solve Time: 0.1051 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0074734 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20921 s | Solve Time: 0.108065 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00854881 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205771 s | Solve Time: 0.126085 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.016396 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.114936 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.70298e+09s, dt:1e+07s, Cycle: 524 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00898747 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.237364 s | Solve Time: 0.0960428 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00669349 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205951 s | Solve Time: 0.111498 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.99e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.016593 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0760553 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.71298e+09s, dt:1e+07s, Cycle: 525 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22339e+07, 2.88795e+07, 4.10314e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.06428e+06, 2.1845e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45776e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.51959e+07, 3.45424e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.30781e+10, 3.35548e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00769e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.30781e+10, 0 }, { 1.59188e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00901094 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219629 s | Solve Time: 0.0924878 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00602817 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205977 s | Solve Time: 0.105786 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0150152 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0916735 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.72298e+09s, dt:1e+07s, Cycle: 526 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00776607 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203116 s | Solve Time: 0.085309 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00888941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204885 s | Solve Time: 0.085196 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00839555 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206513 s | Solve Time: 0.104886 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0128705 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0976915 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.73298e+09s, dt:1.05293e+06s, Cycle: 527 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00694329 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219785 s | Solve Time: 0.0669172 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.94e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0110344 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0102288 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.73403e+09s, dt:1.97143e+06s, Cycle: 528 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00560853 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204573 s | Solve Time: 0.0667544 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.61e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00214634 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0193719 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.736e+09s, dt:3.49189e+06s, Cycle: 529 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.92e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00726597 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203917 s | Solve Time: 0.0892779 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00891763 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208202 s | Solve Time: 0.0873195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00469535 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0338065 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.73949e+09s, dt:5.69929e+06s, Cycle: 530 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00508043 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203749 s | Solve Time: 0.10695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00747333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205563 s | Solve Time: 0.108212 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00866599 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203266 s | Solve Time: 0.105604 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.97e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.67e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0057795 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0498543 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.74519e+09s, dt:8.55517e+06s, Cycle: 531 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00653974 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208081 s | Solve Time: 0.0873591 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00743023 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209275 s | Solve Time: 0.111397 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00873771 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206898 s | Solve Time: 0.104707 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00508673 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209624 s | Solve Time: 0.167796 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00956849 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0571182 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.75375e+09s, dt:1e+07s, Cycle: 532 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00542199 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203253 s | Solve Time: 0.126396 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.62e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00529712 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206243 s | Solve Time: 0.107894 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00615541 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205278 s | Solve Time: 0.106732 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0153689 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0823409 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.76375e+09s, dt:1e+07s, Cycle: 533 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00717431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219417 s | Solve Time: 0.0883056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00489705 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204519 s | Solve Time: 0.106421 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.06e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0061818 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201775 s | Solve Time: 0.0858955 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00623709 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216193 s | Solve Time: 0.106856 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.24e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0146439 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.104246 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.77375e+09s, dt:1e+07s, Cycle: 534 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.38e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00737035 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21249 s | Solve Time: 0.0877963 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00740234 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21369 s | Solve Time: 0.0892477 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0126274 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0798231 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.78375e+09s, dt:1e+07s, Cycle: 535 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.38e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0060142 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201363 s | Solve Time: 0.105331 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00954054 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202073 s | Solve Time: 0.0854763 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00890917 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201691 s | Solve Time: 0.0862832 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00376089 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205019 s | Solve Time: 0.10589 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.99e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0218433 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0680245 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.79375e+09s, dt:1e+07s, Cycle: 536 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.009104 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206987 s | Solve Time: 0.0872523 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00685293 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20647 s | Solve Time: 0.0884888 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00495613 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203184 s | Solve Time: 0.0876232 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00526434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202978 s | Solve Time: 0.06549 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0260775 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0958831 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.80375e+09s, dt:1e+07s, Cycle: 537 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00729354 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203338 s | Solve Time: 0.106018 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00762121 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208492 s | Solve Time: 0.106711 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00875247 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207821 s | Solve Time: 0.10799 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00782964 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225664 s | Solve Time: 0.0887421 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.03e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0167865 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0715573 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.81375e+09s, dt:1e+07s, Cycle: 538 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00668839 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201189 s | Solve Time: 0.105112 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00780643 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202578 s | Solve Time: 0.087231 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00871405 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203157 s | Solve Time: 0.0864695 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0127008 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0876936 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.82375e+09s, dt:1e+07s, Cycle: 539 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00587641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204607 s | Solve Time: 0.106958 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00714454 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210497 s | Solve Time: 0.111063 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00908316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203074 s | Solve Time: 0.145478 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.08e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00644489 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204129 s | Solve Time: 0.086361 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0083922 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.109438 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.83375e+09s, dt:1e+07s, Cycle: 540 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00644361 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201786 s | Solve Time: 0.148062 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00979214 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205631 s | Solve Time: 0.126566 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00770322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209089 s | Solve Time: 0.105648 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.70e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0103101 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0889235 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.84375e+09s, dt:1e+07s, Cycle: 541 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00569761 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207921 s | Solve Time: 0.113056 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00498849 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203097 s | Solve Time: 0.0862814 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00871455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204107 s | Solve Time: 0.088867 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0107386 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0800338 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.85375e+09s, dt:1e+07s, Cycle: 542 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00912376 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201529 s | Solve Time: 0.0863651 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00904809 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202426 s | Solve Time: 0.107025 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00672677 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211535 s | Solve Time: 0.125414 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.15e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0230977 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0767785 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.86375e+09s, dt:1e+07s, Cycle: 543 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22259e+07, 2.88719e+07, 4.10238e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.05562e+06, 2.17476e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45776e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.50197e+07, 3.45426e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.29668e+10, 3.35549e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00768e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.29668e+10, 0 }, { 1.60231e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00415316 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207189 s | Solve Time: 0.129385 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.57e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00588708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205068 s | Solve Time: 0.105054 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00656826 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207691 s | Solve Time: 0.0930096 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0269683 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0638177 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.87375e+09s, dt:1e+07s, Cycle: 544 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00580269 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202425 s | Solve Time: 0.104681 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00913073 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203045 s | Solve Time: 0.0864341 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00704211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20259 s | Solve Time: 0.105582 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0131951 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.068185 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.88375e+09s, dt:1e+07s, Cycle: 545 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.0081655 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204208 s | Solve Time: 0.165698 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00456978 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201766 s | Solve Time: 0.126927 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.01e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0212379 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0659096 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.89375e+09s, dt:1e+07s, Cycle: 546 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00716752 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200846 s | Solve Time: 0.0868085 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00629159 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202533 s | Solve Time: 0.105113 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00938978 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201787 s | Solve Time: 0.124574 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.23e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0224557 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0727581 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.90375e+09s, dt:1e+07s, Cycle: 547 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00695261 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20395 s | Solve Time: 0.0851153 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00563172 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204241 s | Solve Time: 0.110476 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00704476 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204651 s | Solve Time: 0.128595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0128816 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.076637 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.91375e+09s, dt:1e+07s, Cycle: 548 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00618371 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217167 s | Solve Time: 0.108282 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00613187 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203837 s | Solve Time: 0.104475 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.13e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.026651 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0790313 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.92375e+09s, dt:1e+07s, Cycle: 549 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00777494 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200506 s | Solve Time: 0.0852643 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00602487 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203522 s | Solve Time: 0.15024 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0305561 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0823335 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.93375e+09s, dt:1e+07s, Cycle: 550 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00996248 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202483 s | Solve Time: 0.189106 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00506941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204708 s | Solve Time: 0.16922 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.80e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00584848 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205623 s | Solve Time: 0.129814 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0256705 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0720259 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.94375e+09s, dt:1e+07s, Cycle: 551 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0058188 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202566 s | Solve Time: 0.0853346 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.69e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00453285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201274 s | Solve Time: 0.10448 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00471422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202931 s | Solve Time: 0.107615 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00491305 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203727 s | Solve Time: 0.104161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.90e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.90e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00928841 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201582 s | Solve Time: 0.126835 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00736561 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204134 s | Solve Time: 0.126051 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00722669 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213175 s | Solve Time: 0.10555 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0295908 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0589535 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.95375e+09s, dt:1e+07s, Cycle: 552 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00585689 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203428 s | Solve Time: 0.085455 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00455153 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203259 s | Solve Time: 0.085683 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0204336 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0540373 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.96375e+09s, dt:1e+07s, Cycle: 553 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00490007 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202268 s | Solve Time: 0.104819 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0099619 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202083 s | Solve Time: 0.0856821 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00455006 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202637 s | Solve Time: 0.087329 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00935945 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0609218 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.97375e+09s, dt:1e+07s, Cycle: 554 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00711184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202226 s | Solve Time: 0.0850802 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00517574 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224138 s | Solve Time: 0.12723 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0199134 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0693033 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.98375e+09s, dt:1e+07s, Cycle: 555 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00620758 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201547 s | Solve Time: 0.0853062 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0053866 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204277 s | Solve Time: 0.105303 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00457386 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203068 s | Solve Time: 0.127319 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0270643 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0708509 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 4.99375e+09s, dt:1e+07s, Cycle: 556 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00540368 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206725 s | Solve Time: 0.0854758 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00635774 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209381 s | Solve Time: 0.108579 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00615495 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208796 s | Solve Time: 0.106865 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0246256 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0623466 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.00375e+09s, dt:1e+07s, Cycle: 557 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00617439 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215702 s | Solve Time: 0.0910401 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00726303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204733 s | Solve Time: 0.104698 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0180589 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0493212 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.01375e+09s, dt:1e+07s, Cycle: 558 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22195e+07, 2.88656e+07, 4.10164e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.05041e+06, 2.16738e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45776e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.48729e+07, 3.45427e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.28754e+10, 3.35549e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00768e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.28754e+10, 0 }, { 1.61075e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00439555 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201409 s | Solve Time: 0.106521 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00548462 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211564 s | Solve Time: 0.108794 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00962925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221659 s | Solve Time: 0.0872489 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00807211 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0641868 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.02375e+09s, dt:1e+07s, Cycle: 559 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00456126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203236 s | Solve Time: 0.105409 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00889664 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202931 s | Solve Time: 0.0877302 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00833682 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201182 s | Solve Time: 0.125637 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00989412 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.10828 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.03375e+09s, dt:1e+07s, Cycle: 560 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00981611 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205947 s | Solve Time: 0.0857701 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00759414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20858 s | Solve Time: 0.105212 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.98e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00902481 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203543 s | Solve Time: 0.111921 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00909421 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205723 s | Solve Time: 0.108089 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0118878 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.114663 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.04375e+09s, dt:1e+07s, Cycle: 561 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0066443 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205053 s | Solve Time: 0.107657 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00503586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205991 s | Solve Time: 0.107824 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00763649 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206455 s | Solve Time: 0.0873972 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.025469 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0861065 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.05375e+09s, dt:1e+07s, Cycle: 562 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00973219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206982 s | Solve Time: 0.0876972 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00922177 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205583 s | Solve Time: 0.106541 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00458707 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206228 s | Solve Time: 0.107922 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.020389 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0663374 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.06375e+09s, dt:1e+07s, Cycle: 563 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00791362 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203683 s | Solve Time: 0.191897 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.57e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00803056 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203638 s | Solve Time: 0.107565 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00952258 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206557 s | Solve Time: 0.10887 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0255825 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0648281 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.07375e+09s, dt:1e+07s, Cycle: 564 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00989661 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205427 s | Solve Time: 0.10749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00956059 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204222 s | Solve Time: 0.0881734 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00412467 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20475 s | Solve Time: 0.0867874 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.12e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0240782 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0573465 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.08375e+09s, dt:1e+07s, Cycle: 565 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00884246 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206411 s | Solve Time: 0.0854746 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00739523 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20555 s | Solve Time: 0.107459 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00763889 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204842 s | Solve Time: 0.105017 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0154888 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.064476 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.09375e+09s, dt:1e+07s, Cycle: 566 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00816003 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209986 s | Solve Time: 0.0945698 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00841315 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204997 s | Solve Time: 0.0863977 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0065955 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0566451 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.10375e+09s, dt:1e+07s, Cycle: 567 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00455664 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204295 s | Solve Time: 0.111789 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0035049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205535 s | Solve Time: 0.109536 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.50e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0057873 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0501304 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.11375e+09s, dt:1e+07s, Cycle: 568 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00891738 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205415 s | Solve Time: 0.0906771 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00520473 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213023 s | Solve Time: 0.104781 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0093834 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205099 s | Solve Time: 0.0873872 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00604875 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0524113 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.12375e+09s, dt:1e+07s, Cycle: 569 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00555695 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220271 s | Solve Time: 0.107663 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00609422 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207485 s | Solve Time: 0.106312 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0080532 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0604901 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.13375e+09s, dt:1e+07s, Cycle: 570 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00667534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213171 s | Solve Time: 0.10453 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00585641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205901 s | Solve Time: 0.104801 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00571129 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206014 s | Solve Time: 0.105329 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.71e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0149447 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0682436 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.14375e+09s, dt:1e+07s, Cycle: 571 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0092004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220525 s | Solve Time: 0.0868813 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00809311 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205474 s | Solve Time: 0.0853719 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0076171 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204455 s | Solve Time: 0.124764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.019653 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0767415 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.15375e+09s, dt:1e+07s, Cycle: 572 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00721327 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201729 s | Solve Time: 0.0853975 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0086447 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204437 s | Solve Time: 0.0874878 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00408686 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204816 s | Solve Time: 0.128514 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0145346 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0766104 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.16375e+09s, dt:1e+07s, Cycle: 573 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22133e+07, 2.88595e+07, 4.10098e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.04407e+06, 2.16027e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45776e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.47325e+07, 3.45428e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.27879e+10, 3.35549e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00768e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.27879e+10, 0 }, { 1.61882e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00454479 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20252 s | Solve Time: 0.104417 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00378084 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20519 s | Solve Time: 0.107229 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00760031 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205472 s | Solve Time: 0.087453 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00817642 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203825 s | Solve Time: 0.0880286 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0227307 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0697263 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.17375e+09s, dt:1e+07s, Cycle: 574 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00705137 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205931 s | Solve Time: 0.0897091 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00940336 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20992 s | Solve Time: 0.0856555 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00871999 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21507 s | Solve Time: 0.0853141 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00863907 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212204 s | Solve Time: 0.0939388 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.40e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0196791 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0783878 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.18375e+09s, dt:1e+07s, Cycle: 575 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00815862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217384 s | Solve Time: 0.0874488 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00810631 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204557 s | Solve Time: 0.134062 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00945524 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202387 s | Solve Time: 0.10427 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00767888 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204872 s | Solve Time: 0.10501 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00830606 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0678794 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.19375e+09s, dt:1e+07s, Cycle: 576 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00843801 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204607 s | Solve Time: 0.0851345 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00684407 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208086 s | Solve Time: 0.104768 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00290017 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216587 s | Solve Time: 0.106395 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 2.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0148021 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.069441 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.20375e+09s, dt:1e+07s, Cycle: 577 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00669777 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208867 s | Solve Time: 0.104921 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.49e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00661088 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218295 s | Solve Time: 0.10473 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00779376 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203081 s | Solve Time: 0.0709189 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00780446 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.074398 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.21375e+09s, dt:1e+07s, Cycle: 578 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00793088 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203189 s | Solve Time: 0.12557 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00586977 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203333 s | Solve Time: 0.127606 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00700815 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201932 s | Solve Time: 0.0863441 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00794532 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0559266 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.22375e+09s, dt:1e+07s, Cycle: 579 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00413306 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20415 s | Solve Time: 0.104704 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00869843 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203398 s | Solve Time: 0.0851327 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00444004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203993 s | Solve Time: 0.131089 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0030605 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202468 s | Solve Time: 0.0668195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.06e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0171261 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0888441 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.23375e+09s, dt:1e+07s, Cycle: 580 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00405014 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210991 s | Solve Time: 0.107789 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.005538 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204065 s | Solve Time: 0.104622 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0061354 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207027 s | Solve Time: 0.125523 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0177558 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0765253 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.24375e+09s, dt:1e+07s, Cycle: 581 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00397679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206659 s | Solve Time: 0.106359 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-01 ) ; + Last LinSolve(iter,res) = ( 5, 3.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00709601 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205178 s | Solve Time: 0.113792 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00759672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216966 s | Solve Time: 0.10834 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0154042 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0697468 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.25375e+09s, dt:1e+07s, Cycle: 582 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00594971 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21889 s | Solve Time: 0.1103 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.32e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00911397 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203628 s | Solve Time: 0.114664 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0053562 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202102 s | Solve Time: 0.113865 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.36e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0112209 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0833699 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.26375e+09s, dt:1e+07s, Cycle: 583 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00763923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204412 s | Solve Time: 0.115119 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00403411 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224866 s | Solve Time: 0.126087 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00854673 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204817 s | Solve Time: 0.125843 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0186448 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0842828 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.27375e+09s, dt:1e+07s, Cycle: 584 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00806319 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211948 s | Solve Time: 0.107554 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00771535 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213155 s | Solve Time: 0.106545 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00988031 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203563 s | Solve Time: 0.0874634 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0222289 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0683421 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.28375e+09s, dt:1e+07s, Cycle: 585 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00910276 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217072 s | Solve Time: 0.104929 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00656049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207165 s | Solve Time: 0.087071 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00718429 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202552 s | Solve Time: 0.125904 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0186693 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0668189 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.29375e+09s, dt:1e+07s, Cycle: 586 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00661461 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209461 s | Solve Time: 0.104577 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00871644 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202076 s | Solve Time: 0.0652548 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00749538 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228484 s | Solve Time: 0.136496 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.50e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0361516 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0635726 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.30375e+09s, dt:1e+07s, Cycle: 587 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00890296 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21397 s | Solve Time: 0.0852237 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00672661 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203082 s | Solve Time: 0.110944 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00725847 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203307 s | Solve Time: 0.0688218 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0276958 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0546143 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.31375e+09s, dt:1e+07s, Cycle: 588 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22068e+07, 2.88533e+07, 4.10036e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.03669e+06, 2.15282e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45776e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.45902e+07, 3.4543e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.26987e+10, 3.3555e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00767e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.26987e+10, 0 }, { 1.62709e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00561138 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20158 s | Solve Time: 0.107995 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00757144 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204921 s | Solve Time: 0.115544 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00693543 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202369 s | Solve Time: 0.10597 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0057524 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0523985 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.32375e+09s, dt:1e+07s, Cycle: 589 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0093949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201153 s | Solve Time: 0.0852809 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00509942 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204714 s | Solve Time: 0.105428 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.10e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00607158 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0590824 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.33375e+09s, dt:1e+07s, Cycle: 590 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00868923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202099 s | Solve Time: 0.085592 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00630322 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204975 s | Solve Time: 0.106191 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.30e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00475788 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0564156 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.34375e+09s, dt:1e+07s, Cycle: 591 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0087307 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200831 s | Solve Time: 0.0872701 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00806527 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202093 s | Solve Time: 0.104483 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00583721 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201427 s | Solve Time: 0.104648 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00503442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20328 s | Solve Time: 0.104685 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.81e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0122919 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0714879 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.35375e+09s, dt:1e+07s, Cycle: 592 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00507433 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202692 s | Solve Time: 0.106298 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00622808 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201934 s | Solve Time: 0.0909249 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00477155 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203698 s | Solve Time: 0.154512 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0139488 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0833532 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.36375e+09s, dt:1e+07s, Cycle: 593 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00913164 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210633 s | Solve Time: 0.084735 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00518317 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202507 s | Solve Time: 0.110114 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00660168 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211431 s | Solve Time: 0.105416 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0319239 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.078848 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.37375e+09s, dt:1e+07s, Cycle: 594 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00874268 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207975 s | Solve Time: 0.0856304 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00740442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225563 s | Solve Time: 0.110658 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0309712 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0584839 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.38375e+09s, dt:1e+07s, Cycle: 595 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00996214 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220502 s | Solve Time: 0.0856362 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00644707 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206046 s | Solve Time: 0.10594 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00567487 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204655 s | Solve Time: 0.105715 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0204993 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0497677 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.39375e+09s, dt:1e+07s, Cycle: 596 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00935022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203268 s | Solve Time: 0.0884764 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00601124 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20283 s | Solve Time: 0.108206 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00559633 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202946 s | Solve Time: 0.0853762 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0107434 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0559341 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.40375e+09s, dt:1e+07s, Cycle: 597 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00865785 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208165 s | Solve Time: 0.107593 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00752526 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201764 s | Solve Time: 0.105318 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00608008 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0513929 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.41375e+09s, dt:1e+07s, Cycle: 598 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00490297 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204883 s | Solve Time: 0.105047 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00555596 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203021 s | Solve Time: 0.108102 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00854494 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210563 s | Solve Time: 0.0653857 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00391487 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0513686 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.42375e+09s, dt:1e+07s, Cycle: 599 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00712022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200364 s | Solve Time: 0.105043 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0046426 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202072 s | Solve Time: 0.104398 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00319811 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0492907 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.43375e+09s, dt:1e+07s, Cycle: 600 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00631699 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200817 s | Solve Time: 0.104527 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00447743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204931 s | Solve Time: 0.111436 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00341224 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0568186 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.44375e+09s, dt:1e+07s, Cycle: 601 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00969421 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203153 s | Solve Time: 0.0864014 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00544005 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20881 s | Solve Time: 0.108065 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00415749 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0681089 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.45375e+09s, dt:1e+07s, Cycle: 602 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00639839 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223367 s | Solve Time: 0.107506 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0099007 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202188 s | Solve Time: 0.10564 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.27e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00605087 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204123 s | Solve Time: 0.125903 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00607058 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202044 s | Solve Time: 0.125467 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.06e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00601916 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202821 s | Solve Time: 0.125837 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00745362 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0737036 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.46375e+09s, dt:1e+07s, Cycle: 603 +compflowStatistics, reservoir: Pressure (min, average, max): 2.22011e+07, 2.88478e+07, 4.09974e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.03254e+06, 2.14616e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45775e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.44672e+07, 3.45431e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.26225e+10, 3.3555e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00767e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.26225e+10, 0 }, { 1.63411e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00603099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201611 s | Solve Time: 0.104832 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00803117 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230072 s | Solve Time: 0.105662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00407641 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201026 s | Solve Time: 0.0908958 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.08e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00433853 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0643911 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.47375e+09s, dt:1e+07s, Cycle: 604 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00751664 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20488 s | Solve Time: 0.133937 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00863553 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202012 s | Solve Time: 0.125377 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00660168 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202817 s | Solve Time: 0.145479 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00690658 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0726183 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.48375e+09s, dt:1e+07s, Cycle: 605 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00821004 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200814 s | Solve Time: 0.125313 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0041343 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202029 s | Solve Time: 0.106343 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00754207 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203178 s | Solve Time: 0.0874851 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.015443 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0752337 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.49375e+09s, dt:1e+07s, Cycle: 606 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.98e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00622655 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202015 s | Solve Time: 0.124337 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00785105 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204402 s | Solve Time: 0.0853072 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00759274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204279 s | Solve Time: 0.066929 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0175805 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0664738 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.50375e+09s, dt:1e+07s, Cycle: 607 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00594321 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205258 s | Solve Time: 0.127385 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00791562 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224259 s | Solve Time: 0.0872597 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0135114 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0500378 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.51375e+09s, dt:9.28703e+06s, Cycle: 608 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00976941 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207577 s | Solve Time: 0.105191 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00785251 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20804 s | Solve Time: 0.107842 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00472788 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203958 s | Solve Time: 0.125155 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.40e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00872646 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0370687 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.52303e+09s, dt:1e+07s, Cycle: 609 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00714525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214576 s | Solve Time: 0.108092 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00871798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208379 s | Solve Time: 0.112365 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00832358 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207232 s | Solve Time: 0.114008 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00884296 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201243 s | Solve Time: 0.0852484 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00584477 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0729507 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.53303e+09s, dt:1e+07s, Cycle: 610 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00460676 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214328 s | Solve Time: 0.125921 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00638196 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207372 s | Solve Time: 0.104921 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00447336 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0688144 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.54303e+09s, dt:1e+07s, Cycle: 611 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00715912 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206674 s | Solve Time: 0.144863 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00785604 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207495 s | Solve Time: 0.128525 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00962102 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203324 s | Solve Time: 0.108045 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00943874 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202793 s | Solve Time: 0.106459 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00884901 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201522 s | Solve Time: 0.145991 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00592633 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.054509 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.55303e+09s, dt:1e+07s, Cycle: 612 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0051518 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213713 s | Solve Time: 0.149531 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00904068 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224326 s | Solve Time: 0.146512 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.04e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00782863 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207925 s | Solve Time: 0.0958274 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00720575 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0656757 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.56303e+09s, dt:1e+07s, Cycle: 613 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00673996 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208979 s | Solve Time: 0.148294 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.87e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00819624 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206724 s | Solve Time: 0.0672877 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00705735 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0805138 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.57303e+09s, dt:1e+07s, Cycle: 614 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00665591 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205634 s | Solve Time: 0.172661 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00745711 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203278 s | Solve Time: 0.0667445 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.51e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00825673 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0674571 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.58303e+09s, dt:1e+07s, Cycle: 615 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.0083806 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209413 s | Solve Time: 0.229444 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00837385 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20333 s | Solve Time: 0.145494 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.93e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00643723 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0539248 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.59303e+09s, dt:1e+07s, Cycle: 616 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00815927 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20216 s | Solve Time: 0.187624 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.54e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 15 | Final Rel Res: 0.00639568 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210507 s | Solve Time: 0.309684 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.00e-03 ) ; + Last LinSolve(iter,res) = ( 15, 6.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00512323 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0603869 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.60303e+09s, dt:1e+07s, Cycle: 617 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 15 | Final Rel Res: 0.00817628 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203021 s | Solve Time: 0.308222 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-01 ) ; + Last LinSolve(iter,res) = ( 15, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00933522 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2051 s | Solve Time: 0.228048 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00941815 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201885 s | Solve Time: 0.206679 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0115906 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0633723 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.61303e+09s, dt:1e+07s, Cycle: 618 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21957e+07, 2.88426e+07, 4.09919e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.02766e+06, 2.14263e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45775e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.4351e+07, 3.45432e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.25499e+10, 3.3555e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00767e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.25499e+10, 0 }, { 1.64086e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00878115 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.199889 s | Solve Time: 0.247329 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00573556 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212848 s | Solve Time: 0.105465 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00644449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217798 s | Solve Time: 0.105857 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.85e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0241068 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0602204 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.62303e+09s, dt:1e+07s, Cycle: 619 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00611903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216195 s | Solve Time: 0.164854 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00661457 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20179 s | Solve Time: 0.165727 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e+00 ) ; + Last LinSolve(iter,res) = ( 8, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00861946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204458 s | Solve Time: 0.0893763 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.91e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00550534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202293 s | Solve Time: 0.108031 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.21e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00554756 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206679 s | Solve Time: 0.107154 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.55e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0303556 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0516616 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.63303e+09s, dt:1e+07s, Cycle: 620 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00811711 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205846 s | Solve Time: 0.0863219 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00482921 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204947 s | Solve Time: 0.126863 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.83e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0235031 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0395223 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.64303e+09s, dt:1e+07s, Cycle: 621 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00695107 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225405 s | Solve Time: 0.0857512 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00694221 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207589 s | Solve Time: 0.0648632 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.94e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00438823 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0353957 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.65303e+09s, dt:1e+07s, Cycle: 622 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00553098 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201939 s | Solve Time: 0.105399 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00803787 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202095 s | Solve Time: 0.10441 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0040227 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0446411 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.66303e+09s, dt:1e+07s, Cycle: 623 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00970851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204472 s | Solve Time: 0.0870336 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00648903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202187 s | Solve Time: 0.105968 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00611428 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210139 s | Solve Time: 0.0853594 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00405572 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0489162 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.67303e+09s, dt:1e+07s, Cycle: 624 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00580508 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202077 s | Solve Time: 0.106378 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00879371 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204947 s | Solve Time: 0.0650975 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.79e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00423475 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0488108 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.68303e+09s, dt:1e+07s, Cycle: 625 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0097285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217061 s | Solve Time: 0.0855249 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00719928 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202661 s | Solve Time: 0.124993 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.74e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0069358 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0474644 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.69303e+09s, dt:1e+07s, Cycle: 626 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00806008 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214618 s | Solve Time: 0.0884971 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00730476 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206299 s | Solve Time: 0.0870872 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00539391 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208827 s | Solve Time: 0.0680402 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00625923 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0667239 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.70303e+09s, dt:1e+07s, Cycle: 627 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00665163 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220356 s | Solve Time: 0.105919 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00794977 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203766 s | Solve Time: 0.107838 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0132177 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0682693 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.71303e+09s, dt:1e+07s, Cycle: 628 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00802126 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201625 s | Solve Time: 0.124008 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.02e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00940401 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202025 s | Solve Time: 0.0855085 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0179147 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0590177 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.72303e+09s, dt:1e+07s, Cycle: 629 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0087563 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.22152 s | Solve Time: 0.0869591 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00695798 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210948 s | Solve Time: 0.0895576 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0136142 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.045364 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.73303e+09s, dt:1e+07s, Cycle: 630 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00696002 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204077 s | Solve Time: 0.0846424 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00652563 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200265 s | Solve Time: 0.125435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00484048 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202367 s | Solve Time: 0.085926 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00306452 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0470672 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.74303e+09s, dt:1e+07s, Cycle: 631 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00710091 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207755 s | Solve Time: 0.0917173 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0099977 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210693 s | Solve Time: 0.0852961 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 1.00e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00674662 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203869 s | Solve Time: 0.105119 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00697256 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0474808 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.75303e+09s, dt:1e+07s, Cycle: 632 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00765224 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202261 s | Solve Time: 0.0853515 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00920158 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202822 s | Solve Time: 0.105019 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00899869 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202581 s | Solve Time: 0.0661036 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.00e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00901983 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0448322 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.76303e+09s, dt:1e+07s, Cycle: 633 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21903e+07, 2.88375e+07, 4.09866e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.0231e+06, 2.14178e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45775e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.42362e+07, 3.45433e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.24781e+10, 3.3555e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00767e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.24781e+10, 0 }, { 1.64763e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00643058 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201891 s | Solve Time: 0.107405 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00355952 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202966 s | Solve Time: 0.16706 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 8, 3.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00499459 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212912 s | Solve Time: 0.0647877 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0109721 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0602142 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.77303e+09s, dt:1e+07s, Cycle: 634 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00800285 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203062 s | Solve Time: 0.0876052 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00982099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203233 s | Solve Time: 0.124153 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00598731 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203458 s | Solve Time: 0.148998 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00849095 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0844356 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.78303e+09s, dt:1e+07s, Cycle: 635 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00783568 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2036 s | Solve Time: 0.0870453 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00865894 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204167 s | Solve Time: 0.088726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00806749 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204305 s | Solve Time: 0.0847303 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00808322 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0699254 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.79303e+09s, dt:1e+07s, Cycle: 636 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0056486 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203568 s | Solve Time: 0.0946067 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00780261 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203341 s | Solve Time: 0.0862463 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.60e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00699379 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0889067 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.80303e+09s, dt:1e+07s, Cycle: 637 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00595626 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204582 s | Solve Time: 0.113286 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00787833 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207864 s | Solve Time: 0.0899716 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00607295 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206441 s | Solve Time: 0.0890447 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0125745 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0840054 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.81303e+09s, dt:1e+07s, Cycle: 638 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00811883 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213035 s | Solve Time: 0.0886725 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00686929 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209227 s | Solve Time: 0.0882649 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00846925 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208306 s | Solve Time: 0.107821 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.47e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0201661 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0827019 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.82303e+09s, dt:1e+07s, Cycle: 639 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00926869 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218703 s | Solve Time: 0.0966617 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00509321 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205347 s | Solve Time: 0.0848626 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0266601 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.113114 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.83303e+09s, dt:1e+07s, Cycle: 640 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00821439 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202191 s | Solve Time: 0.084724 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0080089 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202098 s | Solve Time: 0.104939 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.01e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0097406 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20189 s | Solve Time: 0.0856976 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0203471 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.112846 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.84303e+09s, dt:1e+07s, Cycle: 641 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00730655 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20776 s | Solve Time: 0.0866149 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.004329 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204272 s | Solve Time: 0.0875282 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00866203 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20343 s | Solve Time: 0.0666661 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0288106 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.07944 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.85303e+09s, dt:1e+07s, Cycle: 642 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00560672 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200438 s | Solve Time: 0.107315 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00556142 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204232 s | Solve Time: 0.0465951 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 2, 5.56e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00429525 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0586238 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.86303e+09s, dt:1e+07s, Cycle: 643 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00552602 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200548 s | Solve Time: 0.104239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00566342 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201869 s | Solve Time: 0.166339 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00414815 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205632 s | Solve Time: 0.166929 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.15e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00446862 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0495423 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.87303e+09s, dt:1e+07s, Cycle: 644 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00585275 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219854 s | Solve Time: 0.107934 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00668828 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206 s | Solve Time: 0.146945 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00563032 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204375 s | Solve Time: 0.144847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00447657 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0397984 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.88303e+09s, dt:1e+07s, Cycle: 645 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00981015 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201728 s | Solve Time: 0.0671826 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00758862 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203778 s | Solve Time: 0.152113 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00454901 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0320065 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.89303e+09s, dt:1e+07s, Cycle: 646 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00446274 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200255 s | Solve Time: 0.0852284 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00982423 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209378 s | Solve Time: 0.0659231 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00396696 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205997 s | Solve Time: 0.167973 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e-04 ) ; + Last LinSolve(iter,res) = ( 8, 3.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00458176 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0512197 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.90303e+09s, dt:1e+07s, Cycle: 647 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00645296 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203948 s | Solve Time: 0.084664 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00865154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203187 s | Solve Time: 0.148083 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.54e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00600729 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0593826 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.91303e+09s, dt:1e+07s, Cycle: 648 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21858e+07, 2.8833e+07, 4.09817e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.01896e+06, 2.14167e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45775e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.41381e+07, 3.45433e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.24173e+10, 3.35551e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00766e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.24173e+10, 0 }, { 1.65342e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00699962 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2052 s | Solve Time: 0.0888709 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00856129 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20564 s | Solve Time: 0.130278 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.56e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00989628 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205829 s | Solve Time: 0.0938824 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.011164 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0653106 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.92303e+09s, dt:1e+07s, Cycle: 649 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00590522 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210078 s | Solve Time: 0.0876144 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00272525 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203656 s | Solve Time: 0.105292 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 5, 2.73e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0159088 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0624601 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.93303e+09s, dt:1e+07s, Cycle: 650 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00663323 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.199892 s | Solve Time: 0.124387 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00977346 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203493 s | Solve Time: 0.106337 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.77e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00933067 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.058204 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.94303e+09s, dt:1e+07s, Cycle: 651 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00562147 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.230395 s | Solve Time: 0.128345 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00660372 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201131 s | Solve Time: 0.145842 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.39e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0173829 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0517498 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.95303e+09s, dt:1e+07s, Cycle: 652 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00959338 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201485 s | Solve Time: 0.124206 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00382184 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201393 s | Solve Time: 0.165045 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 8, 3.82e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00992556 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205763 s | Solve Time: 0.111489 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00599098 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201405 s | Solve Time: 0.144174 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00821728 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213049 s | Solve Time: 0.131753 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.88e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0204316 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0633992 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.96303e+09s, dt:1e+07s, Cycle: 653 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00488561 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203603 s | Solve Time: 0.103742 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00560069 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210988 s | Solve Time: 0.127299 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.96e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0116497 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0563928 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.97303e+09s, dt:1e+07s, Cycle: 654 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00998554 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202448 s | Solve Time: 0.107242 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00591652 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202474 s | Solve Time: 0.145315 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.92e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00536644 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204693 s | Solve Time: 0.148291 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00521781 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203473 s | Solve Time: 0.145246 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.22e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00318979 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.043585 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.98303e+09s, dt:1e+07s, Cycle: 655 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00736751 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210405 s | Solve Time: 0.0873247 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00667515 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203865 s | Solve Time: 0.150994 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00284122 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0378671 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 5.99303e+09s, dt:1e+07s, Cycle: 656 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00811448 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200926 s | Solve Time: 0.0910726 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00948753 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214652 s | Solve Time: 0.0844895 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0053787 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201656 s | Solve Time: 0.124785 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.38e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00539015 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201783 s | Solve Time: 0.125022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.25e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00648898 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0467357 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.00303e+09s, dt:1e+07s, Cycle: 657 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00449282 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203326 s | Solve Time: 0.0855498 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00872556 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212294 s | Solve Time: 0.0876222 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00725022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204798 s | Solve Time: 0.114448 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00592927 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0479463 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.01303e+09s, dt:1e+07s, Cycle: 658 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00736998 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.199937 s | Solve Time: 0.105635 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00637965 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202947 s | Solve Time: 0.0850201 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0086809 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0483276 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.02303e+09s, dt:1e+07s, Cycle: 659 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00381654 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200412 s | Solve Time: 0.105225 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 5, 3.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00640303 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203938 s | Solve Time: 0.116712 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.53e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00639229 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203949 s | Solve Time: 0.104077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00718943 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202109 s | Solve Time: 0.104368 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0092569 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21987 s | Solve Time: 0.124617 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00935139 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209709 s | Solve Time: 0.1477 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00922205 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213959 s | Solve Time: 0.145954 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00950534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205078 s | Solve Time: 0.145015 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00796698 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.228289 s | Solve Time: 0.1457 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.48e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0122772 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0555428 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.03303e+09s, dt:1e+07s, Cycle: 660 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00557739 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225411 s | Solve Time: 0.0894645 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00757311 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206301 s | Solve Time: 0.0863614 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00445553 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208241 s | Solve Time: 0.164962 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.000704651 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211062 s | Solve Time: 0.0254527 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 1, 7.05e-04 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00487692 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0514672 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.04303e+09s, dt:1e+07s, Cycle: 661 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00438504 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202337 s | Solve Time: 0.090373 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00580049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202246 s | Solve Time: 0.147143 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0087623 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210187 s | Solve Time: 0.084307 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00272861 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0427352 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.05303e+09s, dt:1e+07s, Cycle: 662 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00907356 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208145 s | Solve Time: 0.0846282 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00543692 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200878 s | Solve Time: 0.107305 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00704442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205101 s | Solve Time: 0.167512 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.72e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00792823 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0654743 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.06303e+09s, dt:1e+07s, Cycle: 663 +compflowStatistics, reservoir: Pressure (min, average, max): 2.2181e+07, 2.88284e+07, 4.0977e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.01395e+06, 2.13964e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45775e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.40366e+07, 3.45434e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.23538e+10, 3.35551e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00766e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.23538e+10, 0 }, { 1.65957e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00544103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205526 s | Solve Time: 0.105734 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00652503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205115 s | Solve Time: 0.164526 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.29e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.53e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0109779 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.075089 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.07303e+09s, dt:1e+07s, Cycle: 664 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00778121 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20689 s | Solve Time: 0.166016 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.0068484 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214564 s | Solve Time: 0.28839 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 14, 6.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0207778 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0735986 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.08303e+09s, dt:1e+07s, Cycle: 665 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 14 | Final Rel Res: 0.00698434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211871 s | Solve Time: 0.289178 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 14, 6.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00647645 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206822 s | Solve Time: 0.251221 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 12, 6.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0248049 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0614355 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.09303e+09s, dt:1e+07s, Cycle: 666 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 13 | Final Rel Res: 0.0058675 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204997 s | Solve Time: 0.270468 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-01 ) ; + Last LinSolve(iter,res) = ( 13, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00961915 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203371 s | Solve Time: 0.147185 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00785067 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204741 s | Solve Time: 0.165572 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00770843 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200662 s | Solve Time: 0.184565 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.71e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0159992 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0462548 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.10303e+09s, dt:1e+07s, Cycle: 667 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00839209 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202725 s | Solve Time: 0.144227 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00590822 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203705 s | Solve Time: 0.167719 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00826378 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201719 s | Solve Time: 0.124174 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00454235 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0547196 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.11303e+09s, dt:1e+07s, Cycle: 668 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00932104 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200249 s | Solve Time: 0.125644 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00875332 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202447 s | Solve Time: 0.124808 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00814234 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201479 s | Solve Time: 0.104461 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.14e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00733196 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0676991 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.12303e+09s, dt:1e+07s, Cycle: 669 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00679949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219898 s | Solve Time: 0.127358 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.80e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00720047 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206511 s | Solve Time: 0.144721 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00430346 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0653296 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.13303e+09s, dt:1e+07s, Cycle: 670 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00745093 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203167 s | Solve Time: 0.124357 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00647946 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202046 s | Solve Time: 0.165253 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00680823 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0689994 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.14303e+09s, dt:1e+07s, Cycle: 671 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00840879 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200639 s | Solve Time: 0.104213 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00839357 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201279 s | Solve Time: 0.166259 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.56e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00420998 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0620643 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.15303e+09s, dt:1e+07s, Cycle: 672 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0057624 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202469 s | Solve Time: 0.105803 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00639118 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201566 s | Solve Time: 0.147443 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0033337 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0473157 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.16303e+09s, dt:1e+07s, Cycle: 673 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00967262 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211259 s | Solve Time: 0.0878983 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00464735 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202939 s | Solve Time: 0.147151 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00412636 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0679098 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.17303e+09s, dt:1e+07s, Cycle: 674 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00659659 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201118 s | Solve Time: 0.0850073 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0060486 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203721 s | Solve Time: 0.0673443 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00920074 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203901 s | Solve Time: 0.164509 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.93e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.93e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.20e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00727955 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.074538 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.18303e+09s, dt:1e+07s, Cycle: 675 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00615456 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219931 s | Solve Time: 0.0852505 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00721434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203863 s | Solve Time: 0.14448 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.21e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.014792 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0680363 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.19303e+09s, dt:1e+07s, Cycle: 676 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00786562 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207432 s | Solve Time: 0.0906876 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00484852 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206729 s | Solve Time: 0.105826 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00920691 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.049927 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.20303e+09s, dt:1e+07s, Cycle: 677 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00960898 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210218 s | Solve Time: 0.0886755 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00447702 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200959 s | Solve Time: 0.104338 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00302564 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0552773 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.21303e+09s, dt:1e+07s, Cycle: 678 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21764e+07, 2.8824e+07, 4.09724e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.00877e+06, 2.13773e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45775e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.39389e+07, 3.45435e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.22925e+10, 3.35551e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00766e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.22925e+10, 0 }, { 1.66553e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00648011 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20314 s | Solve Time: 0.0876516 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00950104 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20218 s | Solve Time: 0.106562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.50e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00799815 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0584013 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.22303e+09s, dt:1e+07s, Cycle: 679 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00940355 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.199888 s | Solve Time: 0.0845146 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00527557 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21394 s | Solve Time: 0.0849539 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00653679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201283 s | Solve Time: 0.143959 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.013232 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0573897 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.23303e+09s, dt:1e+07s, Cycle: 680 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00575007 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201005 s | Solve Time: 0.104745 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00980491 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200938 s | Solve Time: 0.104276 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00852708 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202394 s | Solve Time: 0.147282 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00742037 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202443 s | Solve Time: 0.165218 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0186289 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0511759 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.24303e+09s, dt:1e+07s, Cycle: 681 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00717551 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203248 s | Solve Time: 0.106097 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.87e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.0080277 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203958 s | Solve Time: 0.145778 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00972098 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203153 s | Solve Time: 0.165783 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.72e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0194776 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0414902 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.25303e+09s, dt:1e+07s, Cycle: 682 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00557219 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201463 s | Solve Time: 0.106149 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00953503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201465 s | Solve Time: 0.125195 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00942244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211879 s | Solve Time: 0.165677 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00794936 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201646 s | Solve Time: 0.165552 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00538157 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0519285 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.26303e+09s, dt:1e+07s, Cycle: 683 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00983715 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202548 s | Solve Time: 0.146634 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00745886 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202131 s | Solve Time: 0.16659 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00354292 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215753 s | Solve Time: 0.165238 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 8, 3.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00513652 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0676819 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.27303e+09s, dt:1e+07s, Cycle: 684 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00538957 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203626 s | Solve Time: 0.187451 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.23e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.39e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0076019 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20525 s | Solve Time: 0.108188 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00557032 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.214129 s | Solve Time: 0.144374 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00405502 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205577 s | Solve Time: 0.126229 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.54e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.54e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.06e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0040505 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0802592 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.28303e+09s, dt:1e+07s, Cycle: 685 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00877586 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20533 s | Solve Time: 0.0862022 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00952425 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201038 s | Solve Time: 0.104712 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00689117 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206844 s | Solve Time: 0.0859851 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00383892 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0782783 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.29303e+09s, dt:1e+07s, Cycle: 686 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00808877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205934 s | Solve Time: 0.105574 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00688835 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204944 s | Solve Time: 0.169113 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.89e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00381756 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0640378 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.30303e+09s, dt:9.0048e+06s, Cycle: 687 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00970374 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205544 s | Solve Time: 0.0853531 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00661727 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206714 s | Solve Time: 0.105562 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00653567 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0559527 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.31204e+09s, dt:1e+07s, Cycle: 688 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00884339 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216771 s | Solve Time: 0.10592 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00902735 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20209 s | Solve Time: 0.106595 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00633688 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201265 s | Solve Time: 0.14503 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 0.00823344 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200608 s | Solve Time: 0.0260616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-04 ) ; + Last LinSolve(iter,res) = ( 1, 8.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00746635 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0691631 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.32204e+09s, dt:1e+07s, Cycle: 689 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00655276 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201574 s | Solve Time: 0.0851179 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00741674 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216312 s | Solve Time: 0.0657083 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 8 | Final Rel Res: 0.00896288 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207929 s | Solve Time: 0.167664 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.86e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.86e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.96e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0190556 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0705535 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.33204e+09s, dt:1e+07s, Cycle: 690 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00883877 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209741 s | Solve Time: 0.0915924 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00933503 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218521 s | Solve Time: 0.0644749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.34e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00513477 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216862 s | Solve Time: 0.124865 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.22e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0301139 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0630938 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.34204e+09s, dt:1e+07s, Cycle: 691 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00964211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204976 s | Solve Time: 0.0851912 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.64e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00669913 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201892 s | Solve Time: 0.126971 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.70e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.025636 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0680241 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.35204e+09s, dt:1e+07s, Cycle: 692 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00648333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202466 s | Solve Time: 0.0847068 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00954017 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201841 s | Solve Time: 0.0653596 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.05e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.54e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0123012 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0710445 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.36204e+09s, dt:1e+07s, Cycle: 693 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21718e+07, 2.88194e+07, 4.09678e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.00484e+06, 2.13524e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45774e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.38402e+07, 3.45436e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.22301e+10, 3.35551e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00766e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.22301e+10, 0 }, { 1.67162e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00523826 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200761 s | Solve Time: 0.104722 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00672687 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203894 s | Solve Time: 0.085967 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00447083 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0709807 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.37204e+09s, dt:1e+07s, Cycle: 694 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00616266 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209345 s | Solve Time: 0.105945 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00839851 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200751 s | Solve Time: 0.0848285 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00374407 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0558987 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.38204e+09s, dt:1e+07s, Cycle: 695 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00570167 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201739 s | Solve Time: 0.10643 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00993545 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208489 s | Solve Time: 0.0848021 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00356471 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216453 s | Solve Time: 0.125589 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 6, 3.56e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00420705 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0453854 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.39204e+09s, dt:1e+07s, Cycle: 696 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00798589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201676 s | Solve Time: 0.0856879 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00926363 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203615 s | Solve Time: 0.109161 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00690832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20059 s | Solve Time: 0.125433 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00457873 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20104 s | Solve Time: 0.10496 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.58e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00447872 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0427288 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.40204e+09s, dt:1e+07s, Cycle: 697 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00760901 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217447 s | Solve Time: 0.0856334 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00818621 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21881 s | Solve Time: 0.0841214 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0050699 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.065718 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.41204e+09s, dt:1e+07s, Cycle: 698 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00557449 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200497 s | Solve Time: 0.0856623 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00599938 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202107 s | Solve Time: 0.125971 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00722864 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203349 s | Solve Time: 0.0880686 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0120536 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0692855 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.42204e+09s, dt:1e+07s, Cycle: 699 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00611153 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.225319 s | Solve Time: 0.0867264 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00598603 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210185 s | Solve Time: 0.104775 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119391 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0630647 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.43204e+09s, dt:1e+07s, Cycle: 700 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00545343 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20085 s | Solve Time: 0.0843295 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00687577 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21853 s | Solve Time: 0.104529 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0119074 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0839003 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.44204e+09s, dt:1e+07s, Cycle: 701 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00609431 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211812 s | Solve Time: 0.0864009 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00574916 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20169 s | Solve Time: 0.126882 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00894674 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210711 s | Solve Time: 0.0673064 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.95e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0164335 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.076949 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.45204e+09s, dt:1e+07s, Cycle: 702 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00881089 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201826 s | Solve Time: 0.085843 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0057174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2059 s | Solve Time: 0.107341 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.07e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0164545 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0571793 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.46204e+09s, dt:1e+07s, Cycle: 703 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00567168 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202248 s | Solve Time: 0.0854196 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00766236 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204812 s | Solve Time: 0.105574 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0218405 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0494786 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.47204e+09s, dt:1e+07s, Cycle: 704 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00817882 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205279 s | Solve Time: 0.0862959 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0051526 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204592 s | Solve Time: 0.107739 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00959602 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202959 s | Solve Time: 0.088122 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0131143 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0474618 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.48204e+09s, dt:1e+07s, Cycle: 705 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00826614 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.222774 s | Solve Time: 0.0867532 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.0043962 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20342 s | Solve Time: 0.126763 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.40e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00507091 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.04582 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.49204e+09s, dt:1e+07s, Cycle: 706 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00541911 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202205 s | Solve Time: 0.0849529 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0093833 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202518 s | Solve Time: 0.106457 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00499897 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0411783 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.50204e+09s, dt:1e+07s, Cycle: 707 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00518499 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211336 s | Solve Time: 0.0911641 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00785465 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208012 s | Solve Time: 0.127244 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00872483 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203323 s | Solve Time: 0.0659318 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.72e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00515291 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0391251 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.51204e+09s, dt:1e+07s, Cycle: 708 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21681e+07, 2.88159e+07, 4.09637e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.00206e+06, 2.13348e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45774e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.37629e+07, 3.45437e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.21822e+10, 3.35552e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00765e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.21822e+10, 0 }, { 1.6763e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00721201 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.199514 s | Solve Time: 0.0847411 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00398049 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20076 s | Solve Time: 0.103823 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.98e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00473526 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0493835 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.52204e+09s, dt:1e+07s, Cycle: 709 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00535791 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203858 s | Solve Time: 0.20922 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.36e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00897052 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21949 s | Solve Time: 0.105433 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.97e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00468623 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0567637 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.53204e+09s, dt:1e+07s, Cycle: 710 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00613209 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201833 s | Solve Time: 0.188104 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.00588921 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202547 s | Solve Time: 0.205358 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 10 | Final Rel Res: 0.0059381 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201846 s | Solve Time: 0.209625 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.94e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 11 | Final Rel Res: 0.00579347 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20248 s | Solve Time: 0.23518 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.22e-04 ) ; + Last LinSolve(iter,res) = ( 11, 5.79e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00464112 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.060821 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.54204e+09s, dt:1e+07s, Cycle: 711 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00657679 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206388 s | Solve Time: 0.185969 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00956519 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224903 s | Solve Time: 0.125623 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.57e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00725886 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.216403 s | Solve Time: 0.128578 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0126924 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0586062 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.55204e+09s, dt:1e+07s, Cycle: 712 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00969945 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201013 s | Solve Time: 0.106135 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.70e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00696446 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206211 s | Solve Time: 0.107199 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00606761 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20146 s | Solve Time: 0.104023 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00918335 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201147 s | Solve Time: 0.0451869 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0072848 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0582622 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.56204e+09s, dt:1e+07s, Cycle: 713 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00715339 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.221664 s | Solve Time: 0.085399 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0045333 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220761 s | Solve Time: 0.104394 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.53e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00856982 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205382 s | Solve Time: 0.0451801 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0114907 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0610698 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.57204e+09s, dt:1e+07s, Cycle: 714 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0060461 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204998 s | Solve Time: 0.0883896 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00588419 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203851 s | Solve Time: 0.106837 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0163798 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0561327 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.58204e+09s, dt:1e+07s, Cycle: 715 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00497031 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.210708 s | Solve Time: 0.0860119 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00610705 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20248 s | Solve Time: 0.104383 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0182056 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0504902 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.59204e+09s, dt:1e+07s, Cycle: 716 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00797979 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202433 s | Solve Time: 0.0853364 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00729584 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20642 s | Solve Time: 0.105323 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.30e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0219315 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0631939 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.60204e+09s, dt:1e+07s, Cycle: 717 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00818715 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20093 s | Solve Time: 0.0849192 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00692935 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200932 s | Solve Time: 0.0648225 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.93e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0259679 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0638336 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.61204e+09s, dt:1e+07s, Cycle: 718 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00441716 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21657 s | Solve Time: 0.107049 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0048381 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209701 s | Solve Time: 0.106996 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0092484 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202264 s | Solve Time: 0.0888446 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00549838 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0455208 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.62204e+09s, dt:1e+07s, Cycle: 719 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00503046 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200962 s | Solve Time: 0.125083 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.03e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00404429 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201348 s | Solve Time: 0.146175 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.04e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00534288 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0407297 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.63204e+09s, dt:1e+07s, Cycle: 720 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00511932 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.218828 s | Solve Time: 0.109421 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00471501 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.224507 s | Solve Time: 0.126436 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.72e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0087841 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206104 s | Solve Time: 0.0705823 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.78e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0118068 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0467007 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.64204e+09s, dt:1e+07s, Cycle: 721 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00908551 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209867 s | Solve Time: 0.0874624 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00502001 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209888 s | Solve Time: 0.0649769 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00618492 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.079625 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.65204e+09s, dt:1e+07s, Cycle: 722 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00883797 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204461 s | Solve Time: 0.084736 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00613747 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202833 s | Solve Time: 0.0652975 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.14e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00904704 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200784 s | Solve Time: 0.104298 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00416352 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0656861 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.66204e+09s, dt:1e+07s, Cycle: 723 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21638e+07, 2.88117e+07, 4.09597e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.9983e+06, 2.13141e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45774e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.36731e+07, 3.45437e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.21255e+10, 3.35552e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00765e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.21255e+10, 0 }, { 1.68188e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00520342 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208612 s | Solve Time: 0.0868011 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00893072 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206413 s | Solve Time: 0.0842331 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00641985 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208063 s | Solve Time: 0.0649258 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.42e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00862915 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0918846 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.67204e+09s, dt:1e+07s, Cycle: 724 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00506154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207516 s | Solve Time: 0.107705 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00620452 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205885 s | Solve Time: 0.106492 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00537248 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205353 s | Solve Time: 0.065261 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0092108 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0783399 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.68204e+09s, dt:1e+07s, Cycle: 725 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00649594 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.220085 s | Solve Time: 0.0854154 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00866364 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203925 s | Solve Time: 0.0872155 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00964948 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200221 s | Solve Time: 0.0846676 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.65e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0136357 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.111027 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.69204e+09s, dt:1e+07s, Cycle: 726 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00645648 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201232 s | Solve Time: 0.0845333 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00423162 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208069 s | Solve Time: 0.105024 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.23e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00659705 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0641153 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.70204e+09s, dt:1e+07s, Cycle: 727 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00478331 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203499 s | Solve Time: 0.0854459 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.38e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00822393 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202537 s | Solve Time: 0.0872361 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00630949 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201653 s | Solve Time: 0.105658 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.31e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00722994 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0609782 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.71204e+09s, dt:1e+07s, Cycle: 728 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00988543 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202099 s | Solve Time: 0.0712907 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.89e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00556534 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203979 s | Solve Time: 0.105599 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00745671 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0547561 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.72204e+09s, dt:1e+07s, Cycle: 729 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00577064 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201609 s | Solve Time: 0.0859999 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00482724 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204932 s | Solve Time: 0.133258 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00589244 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203143 s | Solve Time: 0.0652522 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.89e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0114558 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0474138 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.73204e+09s, dt:1e+07s, Cycle: 730 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00868211 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202162 s | Solve Time: 0.066331 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.68e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00825414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203088 s | Solve Time: 0.105414 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.003995 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201212 s | Solve Time: 0.104854 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.92e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.92e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.99e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0155992 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0642319 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.74204e+09s, dt:1e+07s, Cycle: 731 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00996103 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207317 s | Solve Time: 0.0650154 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00885587 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202275 s | Solve Time: 0.0651157 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0170424 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0547498 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.75204e+09s, dt:1e+07s, Cycle: 732 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00720334 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202543 s | Solve Time: 0.0849734 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00832988 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.217056 s | Solve Time: 0.106844 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.014669 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0822239 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.76204e+09s, dt:1e+07s, Cycle: 733 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 9 | Final Rel Res: 0.00606477 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2181 s | Solve Time: 0.194219 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.06e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00456123 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204117 s | Solve Time: 0.248077 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 12, 4.56e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0137102 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0885218 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.77204e+09s, dt:1e+07s, Cycle: 734 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 12 | Final Rel Res: 0.00568899 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206669 s | Solve Time: 0.251471 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 12, 5.69e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0033676 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20272 s | Solve Time: 0.106836 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.37e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00661228 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203616 s | Solve Time: 0.105145 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00864533 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0653501 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.78204e+09s, dt:1e+07s, Cycle: 735 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00691102 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206164 s | Solve Time: 0.0880753 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0076746 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.212662 s | Solve Time: 0.109504 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.67e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00417548 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0415316 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.79204e+09s, dt:1e+07s, Cycle: 736 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00558054 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205939 s | Solve Time: 0.0889898 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00906202 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201275 s | Solve Time: 0.105301 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.06e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00989028 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0559585 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.80204e+09s, dt:1e+07s, Cycle: 737 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0073255 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207104 s | Solve Time: 0.0851642 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00442896 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.207927 s | Solve Time: 0.10656 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.43e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0106658 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.052396 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.81204e+09s, dt:1e+07s, Cycle: 738 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21593e+07, 2.88073e+07, 4.09554e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.99428e+06, 2.12815e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45774e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.35786e+07, 3.45438e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.20653e+10, 3.35552e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00765e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.20653e+10, 0 }, { 1.68783e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00754261 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215209 s | Solve Time: 0.0925599 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00538741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204687 s | Solve Time: 0.107482 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00544822 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0468475 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.82204e+09s, dt:1e+07s, Cycle: 739 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00854642 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215023 s | Solve Time: 0.0858847 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00695987 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201487 s | Solve Time: 0.128486 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00568455 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201105 s | Solve Time: 0.064867 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.68e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00417641 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0532761 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.83204e+09s, dt:1e+07s, Cycle: 740 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00863021 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204037 s | Solve Time: 0.088711 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00435199 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201488 s | Solve Time: 0.104779 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.37e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.35e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0044877 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0673653 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.84204e+09s, dt:1e+07s, Cycle: 741 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00600059 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.227972 s | Solve Time: 0.0914227 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00485099 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204688 s | Solve Time: 0.125648 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.85e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0065103 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0570527 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.85204e+09s, dt:1e+07s, Cycle: 742 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00667048 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20643 s | Solve Time: 0.0852889 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00543989 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223899 s | Solve Time: 0.10459 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00752321 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.059277 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.86204e+09s, dt:1e+07s, Cycle: 743 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00690162 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206463 s | Solve Time: 0.0859838 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00546446 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204741 s | Solve Time: 0.12819 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.46e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0044893 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0495452 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.87204e+09s, dt:1e+07s, Cycle: 744 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00615843 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204669 s | Solve Time: 0.0853748 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00480764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215541 s | Solve Time: 0.086439 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00743891 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0803882 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.88204e+09s, dt:1e+07s, Cycle: 745 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.007736 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.208636 s | Solve Time: 0.085443 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00568923 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.209993 s | Solve Time: 0.105246 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00523923 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0740102 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.89204e+09s, dt:1e+07s, Cycle: 746 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00696174 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20296 s | Solve Time: 0.085506 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00381157 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200386 s | Solve Time: 0.124603 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.49e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.81e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00948578 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0602665 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.90204e+09s, dt:1e+07s, Cycle: 747 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00472532 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20263 s | Solve Time: 0.0853221 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00437019 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203485 s | Solve Time: 0.0886662 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0221275 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0748727 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.91204e+09s, dt:1e+07s, Cycle: 748 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00676262 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201449 s | Solve Time: 0.0864015 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00458264 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201385 s | Solve Time: 0.128141 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.58e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.0075698 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202288 s | Solve Time: 0.0653641 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.57e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0221022 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0655667 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.92204e+09s, dt:1e+07s, Cycle: 749 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00561652 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204441 s | Solve Time: 0.0859268 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00873741 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201116 s | Solve Time: 0.0861317 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0150237 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0501631 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.93204e+09s, dt:1e+07s, Cycle: 750 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0094468 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.21067 s | Solve Time: 0.105205 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00762943 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202738 s | Solve Time: 0.105154 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.63e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0087383 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0486248 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.94204e+09s, dt:1e+07s, Cycle: 751 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0051167 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219767 s | Solve Time: 0.105953 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.12e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.0095469 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204449 s | Solve Time: 0.105822 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.55e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00498834 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0544789 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.95204e+09s, dt:1e+07s, Cycle: 752 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00782743 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202409 s | Solve Time: 0.10763 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.83e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00645442 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.219776 s | Solve Time: 0.0858819 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00524434 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203758 s | Solve Time: 0.0677061 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.24e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00422221 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0506593 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.96204e+09s, dt:1e+07s, Cycle: 753 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21552e+07, 2.88033e+07, 4.09512e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.99007e+06, 2.12493e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45774e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.34929e+07, 3.45439e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 2.20107e+10, 3.35552e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00765e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2.20107e+10, 0 }, { 1.69324e+10, 3.35483e+13 } } kg +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00965341 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.213939 s | Solve Time: 0.0857316 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00510903 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20519 s | Solve Time: 0.107912 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00845332 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206832 s | Solve Time: 0.106447 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0045468 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0511726 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.97204e+09s, dt:1e+07s, Cycle: 754 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00620154 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205463 s | Solve Time: 0.0853008 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00580827 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201668 s | Solve Time: 0.125896 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.81e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00901974 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.057014 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.98204e+09s, dt:1e+07s, Cycle: 755 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00516686 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206932 s | Solve Time: 0.104925 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00840968 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206824 s | Solve Time: 0.105264 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00471521 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0550157 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 6.99204e+09s, dt:1e+07s, Cycle: 756 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00899751 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204277 s | Solve Time: 0.10616 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00845232 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20179 s | Solve Time: 0.145192 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.53e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.45e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00427037 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0489471 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.00204e+09s, dt:1e+07s, Cycle: 757 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00748238 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.205352 s | Solve Time: 0.126126 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.29e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.48e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 7 | Final Rel Res: 0.00481298 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204331 s | Solve Time: 0.145166 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.81e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00318505 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0521932 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.01204e+09s, dt:1e+07s, Cycle: 758 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00760348 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203731 s | Solve Time: 0.10624 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00510832 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203436 s | Solve Time: 0.125368 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.11e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00466403 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201384 s | Solve Time: 0.105306 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.32e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.66e-03 ) ; +wellControls: well is shut +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00987284 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0493453 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.02204e+09s, dt:1e+07s, Cycle: 759 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 6 | Final Rel Res: 0.00786414 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203584 s | Solve Time: 0.12945 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00551517 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.203996 s | Solve Time: 0.109137 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00979045 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0491406 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.03204e+09s, dt:1e+07s, Cycle: 760 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00540589 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.215458 s | Solve Time: 0.0879749 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00638 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201972 s | Solve Time: 0.0871828 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.62e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00574823 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0543742 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.04204e+09s, dt:1e+07s, Cycle: 761 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00551475 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.2271 s | Solve Time: 0.0871204 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00758658 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.206053 s | Solve Time: 0.106435 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.59e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00735495 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0585353 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.05204e+09s, dt:1e+07s, Cycle: 762 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00486097 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.201655 s | Solve Time: 0.0865819 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00717976 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20569 s | Solve Time: 0.0857801 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.011535 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0598605 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.06204e+09s, dt:1e+07s, Cycle: 763 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00646022 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.223911 s | Solve Time: 0.0854736 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00637101 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.200454 s | Solve Time: 0.103992 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.37e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0159364 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0557368 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.07204e+09s, dt:1e+07s, Cycle: 764 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.0061548 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20589 s | Solve Time: 0.0859656 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 4 | Final Rel Res: 0.00702098 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.20705 s | Solve Time: 0.0854086 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0200998 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0470555 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.08204e+09s, dt:1e+07s, Cycle: 765 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-01 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00596215 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.211182 s | Solve Time: 0.105893 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 5 | Final Rel Res: 0.00566415 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.202075 s | Solve Time: 0.107935 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.66e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0199979 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.0434343 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 7.09204e+09s, dt:3.5616e+06s, Cycle: 766 +wellControls: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 3 | Final Rel Res: 0.00435374 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.204819 s | Solve Time: 0.0660308 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.35e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.00274418 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 0.016038 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Cleaning up events +wellControls: well is shut +compositionalMultiphaseReservoirSolver, number of time steps: 767 +compositionalMultiphaseReservoirSolver, number of successful nonlinear iterations: 2519 +compositionalMultiphaseReservoirSolver, number of successful linear iterations: 14336 +compositionalMultiphaseReservoirSolver, number of time step cuts: 0 +compositionalMultiphaseReservoirSolver, number of discarded nonlinear iterations: 0 +compositionalMultiphaseReservoirSolver, number of discarded linear iterations: 0 +Umpire HOST sum across ranks: 7.2 GB +Umpire HOST rank max: 98.7 MB +total time 1385.860s +initialization time 120.890s +run time 1263.686s diff --git a/geos-posp/tests/Data/job_GEOS_825200.out b/geos-posp/tests/Data/job_GEOS_825200.out new file mode 100644 index 00000000..031bb192 --- /dev/null +++ b/geos-posp/tests/Data/job_GEOS_825200.out @@ -0,0 +1,24307 @@ +Num ranks: 1 +MKL max threads: 1 +GEOSX version: 0.2.0 (feature/dkachuma/allow-negative-pressure-with-errors, sha1: d15a5d5) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Started at 2023-06-20 16:04:54 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, SyntheticMesh +Adding Mesh: InternalWell, well_1 +Adding Mesh: InternalWell, well_2 +Adding Mesh: InternalWell, well_3 +Adding Event: PeriodicEvent, outputInjectionPeriod +Adding Event: PeriodicEvent, outputPostInjectionPeriod +Adding Event: PeriodicEvent, statistics +Adding Event: PeriodicEvent, solverApplicationsInjectionPeriod +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod1 +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod2 +Adding Output: VTK, vtkOutput + TableFunction: totalRateTable +Adding Object CellElementRegion named Reservoir from ObjectManager::Catalog. +Adding Object CellElementRegion named Caprock from ObjectManager::Catalog. +Adding Object CellElementRegion named Overburden from ObjectManager::Catalog. +Adding Object CellElementRegion named Underburden from ObjectManager::Catalog. +Adding Object CellElementRegion named Salt from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion1 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion2 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion3 from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: wellControls1_ConstantBHP_table + TableFunction: wellControls1_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table + TableFunction: wellControls2_ConstantBHP_table + TableFunction: wellControls2_ConstantPhaseRate_table + TableFunction: wellControls3_ConstantBHP_table + TableFunction: wellControls3_ConstantPhaseRate_table +VTKMesh 'SyntheticMesh': reading mesh from /scratchrd/GIS/OT/l1094441/TestJeanne/TestJeanne9C/ModelA.vtu +Generating global Ids from VTK mesh +VTKMesh 'SyntheticMesh': generating GEOSX mesh data structure +Importing cell block 0_tetrahedra +Importing cell block 3_tetrahedra +Importing cell block 1_tetrahedra +Importing cell block 4_tetrahedra +Importing cell block 2_tetrahedra +Number of nodes: 9188 + Number of elems: 48935 + C3D4: 48935 +Load balancing: min avg max +(element/rank): 48935 48935 48935 + +++++++++++++++++++++++++++ +InternalWellGenerator = well_1 +MPI rank = 0 + +Number of well elements = 3 +Well element #0 +Coordinates of the element center: { 400, 1400, 237.313 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 400, 1400, -79.354 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 400, 1400, -396.021 } +Next well element # = 1 +No previous well element +First well node: #2 +Second well node: #3 + +Number of perforations = 3 +Perforation #0 +Coordinates of the perforation: { 400, 1400, -15 } +Is connected to well element #1 +Perforation #1 +Coordinates of the perforation: { 400, 1400, -120.436 } +Is connected to well element #1 +Perforation #2 +Coordinates of the perforation: { 400, 1400, -350 } +Is connected to well element #2 + + +++++++++++++++++++++++++++ +InternalWellGenerator = well_2 +MPI rank = 0 + +Number of well elements = 2 +Well element #0 +Coordinates of the element center: { 1200, 742.759, 158.146 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 1200, 742.759, -316.854 } +Next well element # = 0 +No previous well element +First well node: #1 +Second well node: #2 + +Number of perforations = 2 +Perforation #0 +Coordinates of the perforation: { 1200, 742.759, 100 } +Is connected to well element #0 +Perforation #1 +Coordinates of the perforation: { 1200, 742.759, -500 } +Is connected to well element #1 + + +++++++++++++++++++++++++++ +InternalWellGenerator = well_3 +MPI rank = 0 + +Number of well elements = 5 +Well element #0 +Coordinates of the element center: { 800, 1450, 300.646 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 800, 1450, 110.646 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 800, 1450, -79.354 } +Next well element # = 1 +Previous well element #3 +First well node: #2 +Second well node: #3 +Well element #3 +Coordinates of the element center: { 800, 1450, -269.354 } +Next well element # = 2 +Previous well element #4 +First well node: #3 +Second well node: #4 +Well element #4 +Coordinates of the element center: { 800, 1450, -459.354 } +Next well element # = 3 +No previous well element +First well node: #4 +Second well node: #5 + +Number of perforations = 5 +Perforation #0 +Coordinates of the perforation: { 800, 1450, 150 } +Is connected to well element #1 +Perforation #1 +Coordinates of the perforation: { 800, 1450, -30 } +Is connected to well element #2 +Perforation #2 +Coordinates of the perforation: { 800, 1450, -150 } +Is connected to well element #2 +Perforation #3 +Coordinates of the perforation: { 800, 1450, -325 } +Is connected to well element #3 +Perforation #4 +Coordinates of the perforation: { 800, 1450, -480 } +Is connected to well element #4 + +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Caprock, 4_tetrahedra +SyntheticMesh/Level0/Caprock/4_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Caprock/4_tetrahedra/rock_caprock allocated 1 quadrature points +SyntheticMesh/Level0/Caprock/4_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Overburden, 3_tetrahedra +SyntheticMesh/Level0/Overburden/3_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Overburden/3_tetrahedra/rock_burden allocated 1 quadrature points +SyntheticMesh/Level0/Overburden/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Reservoir, 2_tetrahedra +SyntheticMesh/Level0/Reservoir/2_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/2_tetrahedra/rock_reservoir allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Salt, 0_tetrahedra +SyntheticMesh/Level0/Salt/0_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Salt/0_tetrahedra/rock_salt allocated 1 quadrature points +SyntheticMesh/Level0/Salt/0_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Underburden, 1_tetrahedra +SyntheticMesh/Level0/Underburden/1_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Underburden/1_tetrahedra/rock_burden allocated 1 quadrature points +SyntheticMesh/Level0/Underburden/1_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion1, wellRegion1UniqueSubRegion +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion2, wellRegion2UniqueSubRegion +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion3, wellRegion3UniqueSubRegion +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +SyntheticMesh: importing field data from mesh dataset +Time: 0s, dt:100s, Cycle: 0 +compflowStatistics, Reservoir: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.61331e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 0, 6.61331e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 0, 6.38235e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 0, 1.9147e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 0, 4.46764e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 0, 6.38235e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 0, 0 }, { 0, 6.38235e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.29562e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 0, 1.29562e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 0, 1.25037e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 0, 3.7511e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 0, 8.75257e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 0, 1.25037e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 0, 0 }, { 0, 1.25037e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.31585e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 0, 1.31585e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 0, 1.26989e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 0, 3.80968e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 0, 8.88926e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 0, 1.26989e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 0, 0 }, { 0, 1.26989e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.09383e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 0, 1.09383e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 0, 1.05563e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 0, 3.16688e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 0, 7.38938e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 0, 1.05563e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 0, 0 }, { 0, 1.05563e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.31706e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 0, 6.31706e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 0, 6.09645e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 0, 1.82893e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 0, 4.26751e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 0, 6.09645e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 0, 0 }, { 0, 6.09645e+10 } } kg +compflowStatistics: Max phase CFL number: 0.00696878 +compflowStatistics: Max component CFL number: 0.00696878 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.54e+02 ) ; ( R ) = ( 1.54e+02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 7.41e-01 ) ; ( R ) = ( 7.41e-01 ) ; + Last LinSolve(iter,res) = ( 1, 9.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.70e-05 ) ; ( Rwell ) = ( 9.97e-04 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 2, 4.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12337146.157562563 Pa +wellControls1: Total rate: 56.37348443784919 kg/s; total surface volumetric rate: 30.024025669350802 sm3/s +wellControls1: Phase 0 surface volumetric rate: 30.023748128796043 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027754055475897704 sm3/s +wellControls2: BHP (at the specified reference elevation): 13268440.020500632 Pa +wellControls2: Total rate: 56.38455514210006 kg/s; total surface volumetric rate: 30.029921829787227 sm3/s +wellControls2: Phase 0 surface volumetric rate: 30.029644234728664 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002775950585639181 sm3/s +wellControls3: BHP (at the specified reference elevation): 12318458.650753867 Pa +wellControls3: Total rate: 56.379144772078966 kg/s; total surface volumetric rate: 30.027040313946728 sm3/s +wellControls3: Phase 0 surface volumetric rate: 30.02676274552475 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002775684219790799 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.40959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 5.78676e-09 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 100s, dt:200s, Cycle: 1 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 9.97e-04 ) ; ( R ) = ( 1.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.24e-05 ) ; ( Rwell ) = ( 3.96e-06 ) ; ( R ) = ( 9.24e-05 ) ; + Last LinSolve(iter,res) = ( 3, 2.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12310196.482923582 Pa +wellControls1: Total rate: 56.3283651953819 kg/s; total surface volumetric rate: 29.999995554705098 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.99971823628349 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731842161056295 sm3/s +wellControls2: BHP (at the specified reference elevation): 13283621.245611288 Pa +wellControls2: Total rate: 56.328363147049984 kg/s; total surface volumetric rate: 29.999994463781402 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.99971714536988 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184115261253 sm3/s +wellControls3: BHP (at the specified reference elevation): 12227845.268549167 Pa +wellControls3: Total rate: 56.32836414809141 kg/s; total surface volumetric rate: 29.999994996927327 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999717678510873 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184164545015 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.15934 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 1.03308e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 300s, dt:400s, Cycle: 2 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.97e-06 ) ; ( R ) = ( 1.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 5.63e-06 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12321245.117079774 Pa +wellControls1: Total rate: 56.32837354181888 kg/s; total surface volumetric rate: 29.999999999944567 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681481867 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270213385 sm3/s +wellControls2: BHP (at the specified reference elevation): 13381898.728875142 Pa +wellControls2: Total rate: 56.32837354179333 kg/s; total surface volumetric rate: 29.999999999930964 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681468263 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627020005 sm3/s +wellControls3: BHP (at the specified reference elevation): 12261492.207801165 Pa +wellControls3: Total rate: 56.32837354180582 kg/s; total surface volumetric rate: 29.999999999937614 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.99972268147491 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627020722 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.53908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 2.93995e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 700s, dt:800s, Cycle: 3 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 5.63e-06 ) ; ( R ) = ( 3.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-05 ) ; ( Rwell ) = ( 3.22e-06 ) ; ( R ) = ( 3.06e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12362535.831335485 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13510729.712916294 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12317848.1586993 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 3.20584 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 9.42513e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1500s, dt:1600s, Cycle: 4 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 5.40e-06 ) ; ( R ) = ( 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.50e-04 ) ; ( Rwell ) = ( 5.73e-06 ) ; ( R ) = ( 3.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12459883.312855111 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13654363.938479979 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12398787.671024375 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 4.06388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 2.83724e-06 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3100s, dt:3200s, Cycle: 5 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 6.86e-06 ) ; ( R ) = ( 1.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-04 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 2.25e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.27e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12625110.12795745 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 13809003.526953753 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12509514.611810673 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 4.95538 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 1.07892e-05 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6300s, dt:6400s, Cycle: 6 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.05e-05 ) ; ( R ) = ( 1.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 1.43e-05 ) ; ( R ) = ( 5.53e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.33e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12829258.23115572 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 13963944.408440236 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12639439.309444282 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 5.17832 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 6.18038e-05 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 12700s, dt:12649.6s, Cycle: 7 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 1.43e-05 ) ; ( R ) = ( 3.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 1.97e-03 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 1.07e-04 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.13e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.21e-02 ) ; ( Rwell ) = ( 6.93e-04 ) ; ( R ) = ( 8.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.60e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.08e-04 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.67e-05 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-07 ) ; ( Rwell ) = ( 5.77e-09 ) ; ( R ) = ( 1.45e-07 ) ; + Last LinSolve(iter,res) = ( 5, 2.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13130771.101205045 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 14187170.187506337 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12740001.255915536 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 3.97889 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.131086 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 25349.6s, dt:7997.1s, Cycle: 8 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 2.33e-07 ) ; ( R ) = ( 6.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 6.40e-04 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-04 ) ; ( Rwell ) = ( 1.60e-05 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13120649.79607198 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13936023.254895251 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12764351.084337302 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 1.37551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0699892 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 33346.7s, dt:7997.92s, Cycle: 9 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.60e-05 ) ; ( R ) = ( 6.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.72e-04 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 2.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-04 ) ; ( Rwell ) = ( 1.49e-05 ) ; ( R ) = ( 2.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12969574.397761198 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 13606463.097934615 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 12612725.493361548 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.700345 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518183 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 41344.6s, dt:9672.86s, Cycle: 10 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.53e-05 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 9.42e-05 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 2.51e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.50e-05 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-05 ) ; ( Rwell ) = ( 1.62e-07 ) ; ( R ) = ( 2.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12809498.820794523 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 13351577.862489548 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 12359679.454863135 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.593641 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0841619 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 51017.5s, dt:8523.29s, Cycle: 11 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 4.14e-07 ) ; ( R ) = ( 6.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 2.03e-04 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 6.68e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.37e-05 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-04 ) ; ( Rwell ) = ( 8.88e-08 ) ; ( R ) = ( 1.00e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12701900.118431661 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 13087242.032620579 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12208256.724149385 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.56181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676374 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 59540.8s, dt:8719.48s, Cycle: 12 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 4.53e-07 ) ; ( R ) = ( 5.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.22e-04 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 2.59e-06 ) ; ( R ) = ( 5.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12591012.737242643 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12863869.553929575 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12083953.433361951 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.169727 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599951 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 68260.3s, dt:9637.82s, Cycle: 13 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.59e-06 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 2.32e-05 ) ; ( R ) = ( 5.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12505240.031174501 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12695234.469816763 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 11989705.148871938 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051335 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 77898.1s, dt:11721.4s, Cycle: 14 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.55e-06 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 2.04e-05 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.22e-07 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 1.48e-08 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12427105.46233864 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 12551990.88574718 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11892510.764417708 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0823281 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 89619.5s, dt:10489.8s, Cycle: 15 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 1.90e-07 ) ; ( R ) = ( 6.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.52e-05 ) ; ( R ) = ( 5.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 6.98e-07 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12391117.110042347 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12455893.400641864 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11844005.68368829 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.546342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629995 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 100109s, dt:11239.1s, Cycle: 16 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 6.98e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.42e-05 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-04 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 4.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12343238.498298468 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12380406.692840192 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11795370.089504316 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.373457 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0705466 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 111348s, dt:11180.9s, Cycle: 17 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 6.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 2.95e-05 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.32e-06 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.91e-07 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 5.91e-07 ) ; + Last LinSolve(iter,res) = ( 7, 1.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12305008.49662422 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12308717.064979061 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11728720.659626232 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.139568 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0529663 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 122529s, dt:13346s, Cycle: 18 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 5.92e-06 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 2.96e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 5.49e-06 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.15e-05 ) ; ( Rwell ) = ( 3.48e-07 ) ; ( R ) = ( 4.15e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12265776.179160925 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12266921.376007883 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 11664937.219629992 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.590758 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0567987 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 135875s, dt:15265.3s, Cycle: 19 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.20e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 9.29e-06 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 4.49e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.55e-06 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 3.91e-08 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12247764.69903465 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12216892.619307533 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11626157.846513286 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0617914 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 151141s, dt:16559.9s, Cycle: 20 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 5.27e-08 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 1.18e-05 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 5.91e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 8.50e-06 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 2.16e-07 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12241424.274638133 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12172843.474961173 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11625140.911818217 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.614835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0850177 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 167701s, dt:14487.7s, Cycle: 21 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.12e-07 ) ; ( R ) = ( 6.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.16e-05 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 3, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-04 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 2.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12231373.493156876 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12142279.175079811 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 11607947.543207709 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.261335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690862 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 182188s, dt:14614.9s, Cycle: 22 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.24e-06 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.41e-06 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 4.29e-07 ) ; ( R ) = ( 5.98e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12219903.256210728 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 12114155.967614925 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11580433.555529932 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.177384 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0502213 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 196803s, dt:18006.9s, Cycle: 23 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 4.37e-07 ) ; ( R ) = ( 5.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 8.61e-06 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 4.20e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 4.51e-06 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.26e-05 ) ; ( Rwell ) = ( 9.52e-07 ) ; ( R ) = ( 8.26e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12206078.541398471 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12108016.295137031 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11563729.986555003 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.51044 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.086403 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 214810s, dt:15573.9s, Cycle: 24 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 9.52e-07 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 7.23e-06 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.73e-06 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-06 ) ; ( Rwell ) = ( 8.08e-09 ) ; ( R ) = ( 1.21e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12202292.69161467 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12098092.874529993 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11547879.809831511 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.317664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728379 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 230384s, dt:15164.1s, Cycle: 25 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 6.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.65e-05 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.17e-05 ) ; ( Rwell ) = ( 8.43e-07 ) ; ( R ) = ( 5.17e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12205128.955945035 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12087612.902557736 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 11531547.12584477 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0522827 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 245548s, dt:18242.2s, Cycle: 26 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 8.43e-07 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 8.55e-06 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.81e-06 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-06 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 1.26e-06 ) ; + Last LinSolve(iter,res) = ( 4, 1.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12201296.2884513 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 12086379.242075523 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11528273.290812435 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0570903 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 263790s, dt:20799.5s, Cycle: 27 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 5.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 2.78e-05 ) ; ( R ) = ( 6.61e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.39e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 5.46e-06 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 5.82e-07 ) ; ( R ) = ( 7.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12201341.736672416 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12100237.91485237 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 11531489.76063267 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.40259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0806696 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 284590s, dt:18880.9s, Cycle: 28 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 5.82e-07 ) ; ( R ) = ( 6.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 8.56e-06 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 2.44e-06 ) ; ( R ) = ( 4.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12208900.157226218 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12122409.263143126 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11539911.14137693 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.461503 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769527 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 303471s, dt:17708.3s, Cycle: 29 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 2.44e-06 ) ; ( R ) = ( 5.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.70e-05 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 2.19e-06 ) ; ( R ) = ( 7.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12210358.904990789 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12139347.08609162 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11540272.33199013 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0538999 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 321179s, dt:20915.4s, Cycle: 30 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.19e-06 ) ; ( R ) = ( 5.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 1.27e-05 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 6.21e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.83e-06 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 3.50e-07 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12217207.370220903 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12152732.272274297 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 11543024.341771167 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.428054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0717336 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 342095s, dt:20575.7s, Cycle: 31 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 3.50e-07 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 9.31e-06 ) ; ( R ) = ( 6.14e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 4.62e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.17e-03 ) ; ( Rwell ) = ( 1.08e-05 ) ; ( R ) = ( 8.17e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-05 ) ; ( Rwell ) = ( 1.30e-07 ) ; ( R ) = ( 1.21e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12219033.389914662 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 12172191.555568444 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11546799.080707248 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345441 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627033 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 362670s, dt:22112.3s, Cycle: 32 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 6.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 8.38e-06 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.65e-06 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-05 ) ; ( Rwell ) = ( 1.89e-07 ) ; ( R ) = ( 1.20e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12231075.514284937 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 12200679.493881637 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11551577.016415149 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.300057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632143 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 384782s, dt:23640.1s, Cycle: 33 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.04e-06 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 4.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12246814.64845288 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12238501.768077 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11567018.084864957 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.353251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624966 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 408423s, dt:25459.4s, Cycle: 34 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 5.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.77e-02 ) ; ( Rwell ) = ( 4.53e-06 ) ; ( R ) = ( 8.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.69e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 8.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.70e-05 ) ; ( Rwell ) = ( 8.09e-07 ) ; ( R ) = ( 9.70e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12264627.596486025 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12281330.505631603 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11606435.201886138 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.764269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0827001 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 433882s, dt:22712.3s, Cycle: 35 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 8.01e-07 ) ; ( R ) = ( 6.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 5.31e-06 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 7.56e-07 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.37e-06 ) ; ( Rwell ) = ( 2.72e-07 ) ; ( R ) = ( 6.37e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12275936.045081802 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12321955.5705242 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11630547.761646833 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.406801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637147 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 456594s, dt:24158.4s, Cycle: 36 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 2.72e-07 ) ; ( R ) = ( 5.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 9.72e-06 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 6.89e-07 ) ; ( R ) = ( 7.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.39e-05 ) ; ( Rwell ) = ( 7.89e-08 ) ; ( R ) = ( 3.39e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12285313.535306845 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12361397.147042504 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11651866.71159953 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.273299 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565795 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 480753s, dt:27698.7s, Cycle: 37 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 7.89e-08 ) ; ( R ) = ( 5.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 9.83e-06 ) ; ( R ) = ( 7.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 4.87e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 5.95e-06 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.87e-05 ) ; ( Rwell ) = ( 1.86e-07 ) ; ( R ) = ( 3.87e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.04e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12297974.298119027 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12405781.778654108 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 11678346.378868548 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357965 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.100516 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 508451s, dt:21461.4s, Cycle: 38 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; ( R ) = ( 7.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 7.88e-06 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.01e-07 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-06 ) ; ( Rwell ) = ( 6.66e-08 ) ; ( R ) = ( 1.70e-06 ) ; + Last LinSolve(iter,res) = ( 4, 1.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12316155.02447443 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 12440002.321245546 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 11702928.691955293 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.393111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643637 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 529913s, dt:22678.8s, Cycle: 39 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 7.35e-08 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.31e-05 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 1.94e-06 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 6.33e-07 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 2, 9.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12328676.290304588 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12478128.635153437 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 11733526.090022296 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0528202 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 552592s, dt:27115.3s, Cycle: 40 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 6.39e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 3.25e-05 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.03e-06 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-05 ) ; ( Rwell ) = ( 5.73e-08 ) ; ( R ) = ( 4.17e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12339220.143544266 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12518446.969444599 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 11766953.199131487 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367803 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0907127 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 579707s, dt:22647.7s, Cycle: 41 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 6.46e-08 ) ; ( R ) = ( 6.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 2.26e-05 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.25e-07 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-06 ) ; ( Rwell ) = ( 2.68e-08 ) ; ( R ) = ( 3.62e-06 ) ; + Last LinSolve(iter,res) = ( 4, 1.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12347677.706137076 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 12550373.485692844 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11790626.608799871 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604838 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 602355s, dt:24904.9s, Cycle: 42 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.20e-05 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.03e-06 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12362834.044686304 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 12580977.320440948 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 11816220.953301053 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0783041 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 627260s, dt:23079.6s, Cycle: 43 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; ( R ) = ( 5.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 1.05e-05 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 5.24e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.63e-06 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.76e-05 ) ; ( Rwell ) = ( 1.98e-07 ) ; ( R ) = ( 8.76e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12383731.208097566 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 12610695.582851695 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 11846585.118606668 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.477144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0807947 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 650339s, dt:20928s, Cycle: 44 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.05e-07 ) ; ( R ) = ( 6.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 7.83e-06 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-04 ) ; ( Rwell ) = ( 8.85e-07 ) ; ( R ) = ( 2.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12398283.966298103 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12634435.886067819 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11866612.316638183 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.170473 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561499 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 671267s, dt:24108s, Cycle: 45 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 8.76e-07 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 1.22e-05 ) ; ( R ) = ( 8.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 6.34e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 7.90e-06 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.15e-04 ) ; ( Rwell ) = ( 2.63e-07 ) ; ( R ) = ( 2.15e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12414381.624079907 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12664703.27007813 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11887352.638927791 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.391487 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0795173 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 695375s, dt:22104.5s, Cycle: 46 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.69e-07 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 9.96e-06 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.28e-06 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.70e-07 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 5.70e-07 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12432387.694280216 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12688609.363371547 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 11908261.858793287 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.276707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606353 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 717480s, dt:24269s, Cycle: 47 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; ( R ) = ( 5.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.26e-05 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 6.32e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 6.31e-06 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 2.52e-07 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12451499.604383184 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12714730.048355343 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 11929378.973770352 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.361726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728298 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 741749s, dt:23632.1s, Cycle: 48 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.57e-07 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 5.01e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 4.83e-06 ) ; ( R ) = ( 9.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 1.23e-07 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12470411.467630122 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12742731.437458526 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 11956802.943074843 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.626978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669106 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 765381s, dt:24348.5s, Cycle: 49 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 9.38e-06 ) ; ( R ) = ( 4.06e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-04 ) ; ( Rwell ) = ( 7.64e-07 ) ; ( R ) = ( 2.65e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12490127.422193186 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12770864.286273163 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 11979754.244079541 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.293943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688207 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 789729s, dt:24625.1s, Cycle: 50 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 7.70e-07 ) ; ( R ) = ( 6.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.11e-05 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.42e-07 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-06 ) ; ( Rwell ) = ( 6.99e-08 ) ; ( R ) = ( 1.56e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12509134.461597566 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12794861.492555017 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11998267.032977767 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.267228 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599686 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 814354s, dt:27226.2s, Cycle: 51 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 6.70e-08 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 1.70e-05 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 8.28e-07 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12529614.621992538 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12817620.313759927 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12016979.693896176 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.365322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769607 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 841581s, dt:25533.5s, Cycle: 52 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 8.34e-07 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.35e-05 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 6.83e-07 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-06 ) ; ( Rwell ) = ( 5.13e-08 ) ; ( R ) = ( 2.35e-06 ) ; + Last LinSolve(iter,res) = ( 3, 2.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12549971.184365254 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12838144.192098387 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 12037074.4552305 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518598 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 867114s, dt:30866s, Cycle: 53 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 5.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 1.15e-05 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 5.74e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 6.36e-06 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-04 ) ; ( Rwell ) = ( 9.77e-07 ) ; ( R ) = ( 2.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12573403.64955174 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 12868769.289469818 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12069161.634467982 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.647297 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640486 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 897980s, dt:32720.6s, Cycle: 54 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 9.80e-07 ) ; ( R ) = ( 5.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.00e-05 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.19e-07 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-06 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 2.38e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12598123.730083294 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 12900655.619589217 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12097720.108980944 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.397388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0943531 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 930701s, dt:26560.3s, Cycle: 55 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 7.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 2.95e-05 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.09e-07 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.36e-07 ) ; ( Rwell ) = ( 9.94e-09 ) ; ( R ) = ( 6.36e-07 ) ; + Last LinSolve(iter,res) = ( 5, 5.37e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12621977.489585243 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 12925620.49873713 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12119152.52720531 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.398825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716018 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 957261s, dt:26161.2s, Cycle: 56 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 7.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.92e-05 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.52e-07 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.44e-07 ) ; ( Rwell ) = ( 7.34e-09 ) ; ( R ) = ( 8.44e-07 ) ; + Last LinSolve(iter,res) = ( 5, 2.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12641294.968619782 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12947112.826718764 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12136411.107143389 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.193761 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0590968 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 983422s, dt:29192.6s, Cycle: 57 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 7.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.25e-05 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 5.85e-07 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-05 ) ; ( Rwell ) = ( 5.56e-08 ) ; ( R ) = ( 1.06e-05 ) ; + Last LinSolve(iter,res) = ( 2, 6.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12661267.84399922 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12969502.358913276 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12156066.849880021 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.368153 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0802112 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.01261e+06s, dt:26605.2s, Cycle: 58 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 6.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.38e-05 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 7.38e-07 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12679452.46134544 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12989572.12966096 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12175042.022970038 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.297116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686522 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03922e+06s, dt:26951.2s, Cycle: 59 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 7.41e-07 ) ; ( R ) = ( 6.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 1.17e-05 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 5.95e-07 ) ; ( R ) = ( 5.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12701498.607656274 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 13011245.151056368 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12196944.605860006 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.33519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0610078 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.06617e+06s, dt:29475.5s, Cycle: 60 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 5.98e-07 ) ; ( R ) = ( 6.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 1.74e-05 ) ; ( R ) = ( 7.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 8.62e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.73e-05 ) ; ( Rwell ) = ( 5.45e-07 ) ; ( R ) = ( 4.73e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12732558.981495058 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 13036804.937833631 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12227017.36245946 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.467828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728617 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.09565e+06s, dt:28693.5s, Cycle: 61 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 5.37e-07 ) ; ( R ) = ( 6.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.64e-05 ) ; ( R ) = ( 5.33e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 6.07e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.90e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12760178.762729296 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13061610.719050955 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12256241.954657773 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.408467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0714306 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.12434e+06s, dt:28307.8s, Cycle: 62 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.35e-05 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.30e-07 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12783977.547966564 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13085737.172500346 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12282394.005817333 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632688 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15265e+06s, dt:30246.8s, Cycle: 63 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 6.33e-07 ) ; ( R ) = ( 6.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 9.26e-06 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 4.95e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 1.15e-05 ) ; ( R ) = ( 7.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.97e-05 ) ; ( Rwell ) = ( 5.72e-07 ) ; ( R ) = ( 5.97e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12808026.528146418 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13111720.07572803 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12310253.398490662 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.430615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613937 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18289e+06s, dt:32947.3s, Cycle: 64 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 5.65e-07 ) ; ( R ) = ( 6.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 7.60e-06 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12834408.551860178 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13138789.33626655 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12336562.239663858 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.300551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723245 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.21584e+06s, dt:32233.7s, Cycle: 65 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 6.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 1.98e-05 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.79e-07 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-06 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 1.88e-06 ) ; + Last LinSolve(iter,res) = ( 3, 2.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12857394.946645504 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 13163981.346056897 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12359309.219390113 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.211322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059703 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.24808e+06s, dt:35738.5s, Cycle: 66 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 6.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 2.18e-05 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.09e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.58e-06 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12887374.948878696 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13195159.656043798 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12391185.169738056 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.374445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0717555 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.28381e+06s, dt:35150.8s, Cycle: 67 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 2.81e-05 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-04 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 3.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12918513.639511287 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13224581.746866737 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12424443.123457063 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0760672 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.31896e+06s, dt:33230.6s, Cycle: 68 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 6.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.72e-05 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 7.87e-07 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.11e-06 ) ; ( Rwell ) = ( 1.60e-07 ) ; ( R ) = ( 4.11e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12944100.778878445 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13252254.903222507 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12453020.390070518 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.366791 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641019 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.3522e+06s, dt:35208.4s, Cycle: 69 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.54e-07 ) ; ( R ) = ( 5.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.20e-05 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.36e-07 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-07 ) ; ( Rwell ) = ( 7.07e-09 ) ; ( R ) = ( 6.55e-07 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12970191.047815965 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13281802.700572215 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12483498.779057475 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.413274 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0733872 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3874e+06s, dt:34108.1s, Cycle: 70 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 6.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.34e-05 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 9.16e-07 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-06 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 2.16e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12998427.934969736 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 13309669.222884776 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12513992.97195591 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.351184 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722513 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.42151e+06s, dt:33392.1s, Cycle: 71 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; ( R ) = ( 6.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.06e-05 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.24e-07 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 2.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-05 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 1.79e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13027627.05407019 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13338000.183257852 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12543330.516170574 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4549e+06s, dt:35064.6s, Cycle: 72 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 7.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.66e-05 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 1.34e-06 ) ; ( R ) = ( 7.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13060155.325777616 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13368628.336166209 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 12574892.387566976 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35213 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645253 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48997e+06s, dt:36993.5s, Cycle: 73 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 1.34e-06 ) ; ( R ) = ( 6.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.47e-05 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-04 ) ; ( Rwell ) = ( 4.43e-07 ) ; ( R ) = ( 1.72e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13092153.632866511 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13400491.547501344 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12606991.971356643 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278018 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0516321 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52696e+06s, dt:44836.9s, Cycle: 74 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 4.47e-07 ) ; ( R ) = ( 6.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 1.56e-05 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 9.35e-07 ) ; ( R ) = ( 6.38e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-05 ) ; ( Rwell ) = ( 8.68e-08 ) ; ( R ) = ( 5.16e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13129619.197478218 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13437741.139278509 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 12645349.36462271 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.384769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0912752 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.5718e+06s, dt:37282.7s, Cycle: 75 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 9.14e-08 ) ; ( R ) = ( 6.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.13e-02 ) ; ( Rwell ) = ( 1.12e-05 ) ; ( R ) = ( 7.13e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.64e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.32e-05 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13160440.127342993 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 13469981.146705272 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 12678579.214447862 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.430766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0801911 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.60908e+06s, dt:33984.3s, Cycle: 76 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 6.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.99e-05 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13187762.131398693 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13499754.292856757 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12708778.778199863 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696726 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.64307e+06s, dt:34090.6s, Cycle: 77 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 6.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.01e-05 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 3.96e-07 ) ; ( R ) = ( 8.47e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13215869.855355034 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13528218.183994727 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 12738946.094332887 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.331686 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606139 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.67716e+06s, dt:37437.1s, Cycle: 78 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 3.99e-07 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.16e-05 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 4.31e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13246728.586013984 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13558790.299118744 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12770061.160242913 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.376986 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0906444 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.71459e+06s, dt:31285.9s, Cycle: 79 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 1.10e-05 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 3.95e-07 ) ; ( R ) = ( 4.80e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13272735.992848968 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13585942.471840788 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12796836.299479937 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369233 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578417 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.74588e+06s, dt:35383s, Cycle: 80 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.98e-07 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.46e-05 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-04 ) ; ( Rwell ) = ( 7.18e-07 ) ; ( R ) = ( 1.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13300823.677502599 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13616453.598649742 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12826230.171938997 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294212 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624271 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.78126e+06s, dt:38133.2s, Cycle: 81 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 7.11e-07 ) ; ( R ) = ( 6.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 1.60e-05 ) ; ( R ) = ( 5.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 1.38e-07 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13331836.623200728 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13648476.467122825 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 12858956.476494333 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.376962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642484 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8194e+06s, dt:40343.1s, Cycle: 82 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.52e-05 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.21e-06 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.40e-05 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 4.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13366539.404852029 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270262836 sm3/s +wellControls2: BHP (at the specified reference elevation): 13681035.10826914 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270262586 sm3/s +wellControls3: BHP (at the specified reference elevation): 12893688.218312168 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.316823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691823 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.85974e+06s, dt:40659.8s, Cycle: 83 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 7.20e-06 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 7.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13400691.87729028 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 13714067.563133286 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 12928157.630033297 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320793 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0554493 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9004e+06s, dt:47200.8s, Cycle: 84 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 6.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.45e-05 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 3.17e-08 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13441315.950165523 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13754149.413672918 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 12969596.094050923 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.49619 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0930372 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.9476e+06s, dt:38708.1s, Cycle: 85 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; ( R ) = ( 6.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 6.78e-06 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-05 ) ; ( Rwell ) = ( 4.59e-08 ) ; ( R ) = ( 3.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13474419.128230102 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13785942.249278821 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 13004701.85062461 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.356482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774588 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.98631e+06s, dt:36140.8s, Cycle: 86 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 7.08e-06 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 8.11e-07 ) ; ( R ) = ( 7.58e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13502612.376966357 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13814994.403738586 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13035573.786488155 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.333766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671496 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.02245e+06s, dt:37149.3s, Cycle: 87 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 8.13e-07 ) ; ( R ) = ( 6.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 8.30e-06 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-04 ) ; ( Rwell ) = ( 4.49e-07 ) ; ( R ) = ( 3.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13531580.408481648 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13844968.101507554 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13066622.307165695 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612134 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.0596e+06s, dt:40542s, Cycle: 88 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 4.49e-07 ) ; ( R ) = ( 6.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 7.31e-06 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 5.72e-07 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13565268.29922534 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13881964.847294748 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13101433.346034376 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.502896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0791822 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.10014e+06s, dt:37281.7s, Cycle: 89 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 6.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 6.97e-06 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-04 ) ; ( Rwell ) = ( 6.23e-07 ) ; ( R ) = ( 3.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13596290.597189061 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 13914754.97479742 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 13133311.989444464 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.301921 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0735307 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.13742e+06s, dt:36068.9s, Cycle: 90 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 6.26e-07 ) ; ( R ) = ( 6.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 9.77e-06 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 4.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13624671.70933674 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13943863.810217032 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 13162005.299108393 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234282 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629464 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17349e+06s, dt:38666.4s, Cycle: 91 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 6.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 1.23e-05 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13653481.825449372 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 13973462.57340018 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls3: BHP (at the specified reference elevation): 13191319.746792123 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.231963 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544964 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.21216e+06s, dt:45364.6s, Cycle: 92 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 6.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 6.54e-06 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.26e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 5.77e-06 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 9.85e-07 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.12e-06 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 2.12e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13687410.066707676 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14008230.158798555 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 13225224.649853665 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.423195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0766927 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.25752e+06s, dt:42646.4s, Cycle: 93 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 6.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 1.27e-05 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 7.82e-07 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.42e-06 ) ; ( Rwell ) = ( 4.85e-08 ) ; ( R ) = ( 6.42e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13718945.919587607 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 14039717.448796796 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13257515.934802111 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274041 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0747813 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.30017e+06s, dt:40789s, Cycle: 94 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 5.25e-08 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 9.42e-06 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-04 ) ; ( Rwell ) = ( 3.28e-07 ) ; ( R ) = ( 3.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13750346.67507955 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14070797.652581695 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 13290371.604571948 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683097 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.34096e+06s, dt:41456.3s, Cycle: 95 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 6.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.15e-06 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-04 ) ; ( Rwell ) = ( 4.82e-07 ) ; ( R ) = ( 3.58e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13783026.73442358 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14104442.4227627 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13324889.902691344 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337444 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640235 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.38241e+06s, dt:43958.4s, Cycle: 96 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 6.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.18e-02 ) ; ( Rwell ) = ( 1.31e-05 ) ; ( R ) = ( 8.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 6.34e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 2.54e-06 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-05 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 2.57e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13820324.246797236 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14140083.155959506 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13363755.165600538 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.434593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0854026 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.42637e+06s, dt:38335s, Cycle: 97 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.69e-07 ) ; ( R ) = ( 6.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 8.31e-06 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-05 ) ; ( Rwell ) = ( 9.64e-07 ) ; ( R ) = ( 7.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13851765.050729394 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 14171151.32454203 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 13396191.236308977 Pa +wellControls3: Total rate: 56.328373541922936 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026309 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.245942 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.081693 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.46471e+06s, dt:34493.7s, Cycle: 98 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 9.66e-07 ) ; ( R ) = ( 6.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 8.27e-06 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.66e-07 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.76e-07 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 5.76e-07 ) ; + Last LinSolve(iter,res) = ( 6, 3.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13880127.634812612 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 14199481.407176144 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13426057.327555688 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343704 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601568 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.4992e+06s, dt:38061.8s, Cycle: 99 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 6.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 6.24e-06 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.54e-05 ) ; ( Rwell ) = ( 4.20e-07 ) ; ( R ) = ( 8.54e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13910737.746928826 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14230934.207834318 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13458208.885140136 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721771 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.53726e+06s, dt:37288.7s, Cycle: 100 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 4.14e-07 ) ; ( R ) = ( 5.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.07e-05 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-04 ) ; ( Rwell ) = ( 4.25e-07 ) ; ( R ) = ( 2.41e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13940297.14323035 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 14260953.926224355 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13488363.249477644 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.238837 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624833 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.57455e+06s, dt:40163.9s, Cycle: 101 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 4.19e-07 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 6.95e-06 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.61e-05 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 5.61e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13971981.904788157 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14292136.034366312 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13520164.94751824 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.350823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061257 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.61471e+06s, dt:43812s, Cycle: 102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 5.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.75e-06 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-04 ) ; ( Rwell ) = ( 3.34e-07 ) ; ( R ) = ( 3.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14006066.985692771 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 14326312.13152389 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 13554873.3469955 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642636 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.65853e+06s, dt:46343.8s, Cycle: 103 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.28e-07 ) ; ( R ) = ( 5.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 6.88e-06 ) ; ( R ) = ( 6.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 3.60e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 3.56e-06 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-05 ) ; ( Rwell ) = ( 6.52e-08 ) ; ( R ) = ( 4.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14042293.195181489 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 14362837.031730963 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 13592279.624629235 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341843 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0573694 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.70487e+06s, dt:52680.9s, Cycle: 104 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 6.52e-08 ) ; ( R ) = ( 5.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 6.02e-06 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 8.78e-08 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.84e-06 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 9.84e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14083946.335352253 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 14405470.85919018 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 13636735.539005922 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.40901 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0864538 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.75755e+06s, dt:45544s, Cycle: 105 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 6.83e-06 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-04 ) ; ( Rwell ) = ( 1.68e-06 ) ; ( R ) = ( 2.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14120639.440438483 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 14442633.964747258 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 13676859.973162431 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0752179 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.8031e+06s, dt:43387.9s, Cycle: 106 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 6.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 7.35e-06 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-04 ) ; ( Rwell ) = ( 7.23e-07 ) ; ( R ) = ( 2.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14155179.006579157 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14477868.857211178 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 13712906.491734624 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.289773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0680674 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.84648e+06s, dt:44201.4s, Cycle: 107 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 7.15e-07 ) ; ( R ) = ( 6.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.72e-06 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 8.94e-08 ) ; ( R ) = ( 4.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14190952.970535275 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 14513687.458788354 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 13750327.485665461 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.287681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0698275 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.89068e+06s, dt:44274.2s, Cycle: 108 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 8.45e-08 ) ; ( R ) = ( 6.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.85e-06 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-04 ) ; ( Rwell ) = ( 9.31e-07 ) ; ( R ) = ( 1.79e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14226437.209085902 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14548797.077120516 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13786950.735190177 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.283262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691958 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.93496e+06s, dt:44615.8s, Cycle: 109 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 9.32e-07 ) ; ( R ) = ( 6.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.46e-06 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 7, 2.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.87e-07 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-05 ) ; ( Rwell ) = ( 1.92e-07 ) ; ( R ) = ( 3.20e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14260963.120797087 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 14584087.261414997 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 13822878.050468406 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639257 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.97957e+06s, dt:47355.4s, Cycle: 110 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 1.95e-07 ) ; ( R ) = ( 6.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 6.11e-06 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 5.58e-07 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14295870.418138325 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14619991.87866204 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 13859118.42962807 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.319821 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065899 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.02693e+06s, dt:49280.2s, Cycle: 111 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 5.51e-07 ) ; ( R ) = ( 5.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 4.87e-06 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 8.85e-07 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 9.86e-08 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14333043.506749043 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 14656277.412526961 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13896739.776498884 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.319943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607209 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.07621e+06s, dt:54057.3s, Cycle: 112 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 9.42e-08 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.56e-06 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.84e-05 ) ; ( Rwell ) = ( 5.55e-07 ) ; ( R ) = ( 9.84e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14374403.93533906 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 14697095.253927981 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13939283.166725334 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.328685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626019 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.13027e+06s, dt:58154.8s, Cycle: 113 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 5.49e-07 ) ; ( R ) = ( 5.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.38e-05 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 9.22e-07 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.79e-05 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 7.79e-05 ) ; + Last LinSolve(iter,res) = ( 7, 1.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14419031.453978155 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14741659.959523382 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13985005.362046823 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.352001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0735571 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.18842e+06s, dt:56249.2s, Cycle: 114 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 9.38e-09 ) ; ( R ) = ( 6.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 9.33e-06 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.80e-07 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.44e-05 ) ; ( Rwell ) = ( 1.46e-07 ) ; ( R ) = ( 5.44e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14461038.094725853 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 14785942.903685559 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 14028286.177444214 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.34241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658974 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.24467e+06s, dt:58536.4s, Cycle: 115 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 4.72e-06 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.79e-08 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.36e-05 ) ; ( Rwell ) = ( 4.60e-08 ) ; ( R ) = ( 1.36e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14503483.181743532 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 14830221.449630735 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 14071845.574096119 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335682 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649749 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.30321e+06s, dt:61478.6s, Cycle: 116 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 6.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 9.31e-06 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-04 ) ; ( Rwell ) = ( 3.09e-07 ) ; ( R ) = ( 3.31e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14546461.43017271 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14874222.418943292 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 14115903.419889962 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.315953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648772 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.36469e+06s, dt:64631.9s, Cycle: 117 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 3.11e-07 ) ; ( R ) = ( 6.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.16e-06 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.32e-06 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-05 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 4.20e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14592280.60914108 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 14920148.438775413 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14163396.169631716 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.372901 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0770153 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.42932e+06s, dt:60584.2s, Cycle: 118 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.09e-07 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.77e-06 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-04 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 2.03e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14635593.515542844 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14962553.76666945 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 14208351.683413707 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313846 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665987 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.4899e+06s, dt:62612.4s, Cycle: 119 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 3.55e-06 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.96e-06 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.85e-05 ) ; ( Rwell ) = ( 2.16e-07 ) ; ( R ) = ( 5.85e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14679775.366461203 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15007953.416913796 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 14254613.718854988 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.382627 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706419 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.55252e+06s, dt:62231.9s, Cycle: 120 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 2.11e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.68e-06 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.24e-03 ) ; ( Rwell ) = ( 3.32e-06 ) ; ( R ) = ( 8.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 4.97e-07 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14724901.524871955 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 15053316.86818153 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 14301877.94020407 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.340615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0765534 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.61475e+06s, dt:58576s, Cycle: 121 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 4.98e-07 ) ; ( R ) = ( 6.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 7.33e-06 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 3.65e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.90e-06 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14767513.046303907 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 15095384.212229079 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 14347334.781352207 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0745105 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.67332e+06s, dt:56163.4s, Cycle: 122 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 2.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14806896.593973778 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15134798.257134553 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 14388226.318145651 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.267376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687868 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.72949e+06s, dt:56819.9s, Cycle: 123 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 2.48e-07 ) ; ( R ) = ( 6.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 5.30e-06 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.43e-05 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 7.43e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14845497.162660463 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15174371.424139135 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 14428271.310072767 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.262481 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633082 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.78631e+06s, dt:60687.6s, Cycle: 124 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 6.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 7.30e-06 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-04 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 1.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 2.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14886369.130445452 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15216811.733596029 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 14470648.647987762 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.366078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065123 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.84699e+06s, dt:63643.7s, Cycle: 125 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 6.29e-06 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.36e-06 ) ; ( Rwell ) = ( 2.18e-08 ) ; ( R ) = ( 4.36e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14930296.54060874 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15261441.356099378 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14516171.12536544 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.344297 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.91064e+06s, dt:67399.1s, Cycle: 126 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; ( R ) = ( 6.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.53e-06 ) ; ( R ) = ( 5.77e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.99e-06 ) ; ( Rwell ) = ( 2.78e-08 ) ; ( R ) = ( 3.99e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.05e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14978483.014090203 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15309098.828152867 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14565610.383124707 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.353691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753576 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.97804e+06s, dt:64127.1s, Cycle: 127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.48e-06 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 9.80e-08 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-06 ) ; ( Rwell ) = ( 3.17e-09 ) ; ( R ) = ( 1.47e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 15023523.308083212 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15354354.729961818 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls3: BHP (at the specified reference elevation): 14611928.998713467 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332301 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730658 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.04216e+06s, dt:62307.8s, Cycle: 128 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 8.03e-09 ) ; ( R ) = ( 6.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.78e-06 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.45e-07 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-06 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 2.51e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15066627.10366838 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15397986.751375867 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 14656971.675511332 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694821 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.10447e+06s, dt:62616.6s, Cycle: 129 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 6.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 1.98e-06 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.00e-07 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.59e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15110520.993386492 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15442245.400847333 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 14702648.399332864 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0700094 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.16709e+06s, dt:62611s, Cycle: 130 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.22e-07 ) ; ( R ) = ( 6.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 5.85e-06 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.37e-05 ) ; ( Rwell ) = ( 4.81e-08 ) ; ( R ) = ( 6.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15154048.924345654 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15486050.860627918 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 14747244.363920579 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.312992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722338 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.2297e+06s, dt:61306.7s, Cycle: 131 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; ( R ) = ( 5.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 2.90e-06 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-04 ) ; ( Rwell ) = ( 3.08e-07 ) ; ( R ) = ( 2.77e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15196385.00532196 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 15528298.00726191 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14790795.371685097 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.323562 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728292 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.29101e+06s, dt:59698.2s, Cycle: 132 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 3.03e-07 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; ( R ) = ( 3.95e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.08e-06 ) ; ( Rwell ) = ( 8.86e-09 ) ; ( R ) = ( 7.08e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15237557.361464653 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15569114.845858028 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 14833193.855662825 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.293958 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688421 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.3507e+06s, dt:60363.9s, Cycle: 133 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; ( R ) = ( 6.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-06 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.23e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15279244.184562733 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 15610106.12646574 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 14875650.371707154 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.301616 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637249 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.41107e+06s, dt:64200.7s, Cycle: 134 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 6.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.19e-06 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 4.94e-07 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.18e-06 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 5.18e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15323629.427804051 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15654055.528772378 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14921693.549978824 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644776 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.47527e+06s, dt:67764.8s, Cycle: 135 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 6.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.98e-06 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 9.97e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15369671.606883293 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15699893.742254697 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 14969476.325854074 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320515 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662952 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.54303e+06s, dt:70243.2s, Cycle: 136 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; ( R ) = ( 6.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 8.51e-07 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15416858.643817697 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15748187.585671792 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15018430.346229922 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721314 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.61328e+06s, dt:68845.8s, Cycle: 137 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 1.85e-07 ) ; ( R ) = ( 6.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.69e-05 ) ; ( Rwell ) = ( 3.45e-07 ) ; ( R ) = ( 7.69e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15462657.482362097 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 15794163.377590818 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 15065700.509505054 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320569 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696781 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.68212e+06s, dt:69057.5s, Cycle: 138 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.05e-04 ) ; ( Rwell ) = ( 2.56e-07 ) ; ( R ) = ( 4.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15508130.240315957 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 15839184.069017056 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 15112151.203341829 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646401 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.75118e+06s, dt:72772.3s, Cycle: 139 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 2.58e-07 ) ; ( R ) = ( 6.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 2.84e-06 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 5.34e-07 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-05 ) ; ( Rwell ) = ( 2.59e-08 ) ; ( R ) = ( 1.86e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15555208.427350774 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15886533.517030891 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15160494.723243712 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.334801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0562203 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.82395e+06s, dt:83765.2s, Cycle: 140 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; ( R ) = ( 6.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 5.84e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-05 ) ; ( Rwell ) = ( 8.11e-09 ) ; ( R ) = ( 1.82e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15608760.789222559 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15940414.481736448 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 15215580.471480945 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.359192 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0892052 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.90772e+06s, dt:70813s, Cycle: 141 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.26e-06 ) ; ( R ) = ( 4.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.83e-06 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 6.83e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15653773.438902719 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 15986974.636191037 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 15262129.6018317 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.322403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687801 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.97853e+06s, dt:71645.4s, Cycle: 142 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; ( R ) = ( 5.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.10e-06 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 2.66e-07 ) ; ( R ) = ( 6.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15698727.924421888 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 16033218.125276769 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15308581.481010806 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294291 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0596002 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.05018e+06s, dt:79521.7s, Cycle: 143 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.68e-07 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 4.55e-06 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.19e-07 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-05 ) ; ( Rwell ) = ( 4.10e-09 ) ; ( R ) = ( 5.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15747881.47755418 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 16083383.570053458 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15359222.951793108 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308101 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627385 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.1297e+06s, dt:85429.9s, Cycle: 144 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 6.53e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.82e-06 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 1.59e-07 ) ; ( R ) = ( 6.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15800485.264042016 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 16136681.863083825 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 15413269.651286839 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.389574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674022 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.21513e+06s, dt:87597.1s, Cycle: 145 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.61e-07 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.07e-06 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 5.58e-07 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 8.76e-09 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15855210.801916944 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 16190887.355444716 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 15469065.18560786 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668393 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.30272e+06s, dt:90315.7s, Cycle: 146 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 8.01e-09 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.58e-06 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.59e-04 ) ; ( Rwell ) = ( 5.97e-08 ) ; ( R ) = ( 3.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15911371.526493661 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16246610.546115935 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 15526354.511404896 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.351983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0902922 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.39304e+06s, dt:75688.2s, Cycle: 147 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 5.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.43e-06 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.72e-07 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15957275.342839258 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 16292870.69317122 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 15573482.008542515 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668366 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.46873e+06s, dt:78039.4s, Cycle: 148 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.92e-06 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16003805.430201665 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 16340068.0379005 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15621348.898785252 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.302937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568969 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.54677e+06s, dt:89166.6s, Cycle: 149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 5.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 1.40e-06 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.70e-06 ) ; ( Rwell ) = ( 4.50e-08 ) ; ( R ) = ( 4.70e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.82e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16056382.024531502 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16393910.994062753 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15675123.485794049 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367065 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653787 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.63593e+06s, dt:93271.7s, Cycle: 150 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; ( R ) = ( 5.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.29e-06 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.79e-07 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.04e-05 ) ; ( Rwell ) = ( 8.09e-08 ) ; ( R ) = ( 5.04e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16112119.793029426 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16450352.945468847 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15732015.211798064 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369294 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0792025 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.72921e+06s, dt:85755.8s, Cycle: 151 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 8.32e-08 ) ; ( R ) = ( 5.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 4.66e-06 ) ; ( R ) = ( 2.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 2.61e-07 ) ; ( R ) = ( 6.31e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16163386.15469336 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16502027.320008637 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15784414.551123235 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.310582 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686688 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.81496e+06s, dt:86857s, Cycle: 152 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.57e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 8.97e-07 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 4.32e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16215746.627679212 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 16553861.516249798 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 15837184.675823225 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.321949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701116 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.90182e+06s, dt:86764.8s, Cycle: 153 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 6.78e-07 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.81e-05 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 6.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16267285.392045256 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16605092.036640229 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 15889495.49939927 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.315183 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671334 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.98858e+06s, dt:89200s, Cycle: 154 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; ( R ) = ( 6.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.20e-06 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 7.64e-08 ) ; ( R ) = ( 8.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16320992.744121088 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 16658642.863658601 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 15944616.019622577 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0751002 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.07778e+06s, dt:85068s, Cycle: 155 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 7.64e-08 ) ; ( R ) = ( 5.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.35e-06 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 8.35e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16372221.520865634 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 16709676.724625992 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 15997275.960209737 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777723 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.16285e+06s, dt:79205s, Cycle: 156 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 1.25e-06 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 6.21e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 6.93e-07 ) ; ( R ) = ( 6.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-05 ) ; ( Rwell ) = ( 7.00e-08 ) ; ( R ) = ( 3.43e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16419690.057989871 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 16757030.48924207 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 16045982.714074152 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279591 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727534 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.24206e+06s, dt:77181.1s, Cycle: 157 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 7.38e-08 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.57e-06 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 8.69e-08 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16464682.23390435 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 16802202.14637973 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 16092031.943406777 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.270981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672504 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.31924e+06s, dt:79256.5s, Cycle: 158 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 8.91e-08 ) ; ( R ) = ( 5.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 7.59e-07 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.82e-03 ) ; ( Rwell ) = ( 1.97e-07 ) ; ( R ) = ( 9.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 3, 3.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16509851.652552592 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16848084.749950267 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 16138346.470788458 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.276336 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0617854 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.39849e+06s, dt:85983.4s, Cycle: 159 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 6.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 4.68e-08 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.69e-05 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 3.69e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.33e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16558430.486321826 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 16897715.948618323 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 16188355.589598557 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.296863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561331 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.48448e+06s, dt:99066.7s, Cycle: 160 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 6.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 7.29e-07 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.05e-06 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 4.05e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16615179.825879112 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 16954182.81430578 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16246607.99882983 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337466 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607346 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.58354e+06s, dt:108655s, Cycle: 161 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 5.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 6.68e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 5.53e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 4.71e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 7.35e-07 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-05 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 1.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16676631.573181104 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17015114.435654465 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16309313.021258594 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.379902 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762995 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.6922e+06s, dt:102505s, Cycle: 162 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 2.01e-06 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-04 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 1.69e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16734186.455653653 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 17072940.690240577 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16368310.643988878 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.350542 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0794866 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.7947e+06s, dt:94011s, Cycle: 163 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.51e-06 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-04 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 1.36e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16787078.71028531 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 17125796.50836143 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 16422379.394209972 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.322028 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0733787 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.88872e+06s, dt:91080.2s, Cycle: 164 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.01e-07 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 2.21e-06 ) ; ( R ) = ( 7.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 1.10e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.58e-07 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.54e-06 ) ; ( Rwell ) = ( 2.82e-09 ) ; ( R ) = ( 3.54e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.86e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 16837404.73399263 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 17176093.019651346 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 16473918.761772873 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666001 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.9798e+06s, dt:94128.1s, Cycle: 165 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; ( R ) = ( 5.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 1.44e-06 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 7.23e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 8.59e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 7.28e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 7.25e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 5.70e-07 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 2.27e-07 ) ; ( R ) = ( 6.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16888156.089273307 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 17227018.837946262 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 16526107.180299439 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.29425 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602306 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.07392e+06s, dt:103784s, Cycle: 166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.28e-07 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.75e-06 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.51e-07 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.08e-07 ) ; ( Rwell ) = ( 7.00e-10 ) ; ( R ) = ( 8.08e-07 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 16943502.39921584 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17282328.1941993 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 16582896.188485742 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619011 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.17771e+06s, dt:112459s, Cycle: 167 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 4.64e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 5.22e-07 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 2.65e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.02e-07 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.18e-05 ) ; ( Rwell ) = ( 1.84e-07 ) ; ( R ) = ( 4.18e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17003178.407949835 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 17342801.47910604 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 16644669.610686496 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346133 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069576 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.29017e+06s, dt:112914s, Cycle: 168 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 5.42e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.76e-08 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-06 ) ; ( Rwell ) = ( 5.04e-09 ) ; ( R ) = ( 1.63e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17064026.22608907 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17404270.37548236 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16707250.028529592 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.347303 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0725904 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.40308e+06s, dt:110196s, Cycle: 169 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 4.65e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 5.17e-07 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17123362.657258365 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 17463428.83284779 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 16767683.216238525 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.318813 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0749344 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.51328e+06s, dt:105250s, Cycle: 170 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.62e-06 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-04 ) ; ( Rwell ) = ( 4.46e-07 ) ; ( R ) = ( 2.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17180169.233131424 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 17519629.026802197 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16825253.305006776 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.340484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.075735 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.61853e+06s, dt:99798.8s, Cycle: 171 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 4.46e-07 ) ; ( R ) = ( 5.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 5.02e-08 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17234076.28164461 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17572968.399522863 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16880038.05687686 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.302115 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0814021 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.71833e+06s, dt:90023s, Cycle: 172 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 4.79e-08 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.82e-06 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 1.44e-07 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.96e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 3.96e-04 ) ; + Last LinSolve(iter,res) = ( 2, 9.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17282536.344845634 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17621616.250400472 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 16929549.777725313 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.28532 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0758887 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.80835e+06s, dt:85242.4s, Cycle: 173 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-04 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 1.05e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17327856.505670793 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17667319.75225472 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 16975761.2700196 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.259496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069401 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.89359e+06s, dt:85731.5s, Cycle: 174 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 7.11e-07 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-05 ) ; ( Rwell ) = ( 7.15e-08 ) ; ( R ) = ( 2.12e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17372695.002812695 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17712305.005370524 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 17021323.916458696 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632554 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.97932e+06s, dt:91616.4s, Cycle: 175 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 6.92e-08 ) ; ( R ) = ( 5.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 5.15e-06 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 1.35e-07 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17419981.107448537 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17759527.780425873 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 17069387.657947436 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266698 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0546621 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.07094e+06s, dt:107289s, Cycle: 176 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 1.45e-06 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 6.57e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.62e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.13e-06 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.91e-07 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-06 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 1.10e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 17475309.357362114 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 17814579.858774222 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 17125696.404909458 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.312175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0526631 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.17823e+06s, dt:128507s, Cycle: 177 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 5.05e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 2.32e-06 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-04 ) ; ( Rwell ) = ( 1.62e-07 ) ; ( R ) = ( 2.74e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17541720.284557555 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 17880594.853958935 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17193256.289509416 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369375 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0576558 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.30673e+06s, dt:145627s, Cycle: 178 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 1.63e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 1.04e-06 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 5.41e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 2.85e-07 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17617293.307911225 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17955997.777289443 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17270297.421035886 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.415802 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0785426 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.45236e+06s, dt:134671s, Cycle: 179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.85e-07 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.26e-06 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 2.41e-07 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17687346.88867736 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 18025593.18997505 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 17341827.58425523 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.381975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777844 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.58703e+06s, dt:125376s, Cycle: 180 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.41e-07 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.98e-06 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 3.41e-07 ) ; ( R ) = ( 7.55e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17751730.759954188 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 18089415.10617658 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17406997.79674083 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.360482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0911079 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.71241e+06s, dt:104390s, Cycle: 181 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.42e-07 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.97e-07 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-06 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 1.46e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17804888.576541513 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 18142333.683897763 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 17461013.463778228 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0801288 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.8168e+06s, dt:95206.2s, Cycle: 182 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 2.13e-06 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-05 ) ; ( Rwell ) = ( 1.14e-07 ) ; ( R ) = ( 6.11e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.46e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17853335.48551722 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 18190787.711830627 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 17510377.286605075 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728816 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.912e+06s, dt:92663.2s, Cycle: 183 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-04 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 1.22e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17900526.389935218 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 18237566.256361365 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 17558463.87807666 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.275992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694347 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.00467e+06s, dt:93164.8s, Cycle: 184 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.17e-07 ) ; ( R ) = ( 5.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.07e-05 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 4.07e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17947858.457768973 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 18284360.796142913 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 17606762.322695814 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281357 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736767 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.09783e+06s, dt:90012.9s, Cycle: 185 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 1.68e-06 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17993222.81800419 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 18329476.225514896 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 17652981.94395687 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0720266 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.18785e+06s, dt:88308.5s, Cycle: 186 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 5.13e-07 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 3.09e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.82e-07 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-06 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 2.47e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18037156.359533917 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 18373293.629240546 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 17697719.093093757 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250426 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664707 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.27615e+06s, dt:91379.9s, Cycle: 187 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 5.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 5.21e-07 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-04 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 2.07e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18081974.5293232 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 18418092.842188805 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17743366.567119647 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588045 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.36753e+06s, dt:102286s, Cycle: 188 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 2.47e-06 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 1.18e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 5.43e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 1.51e-06 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 7.86e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 6.65e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 6.04e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.44e-06 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 7.60e-08 ) ; ( R ) = ( 4.09e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18131809.621656686 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 18468129.947450638 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 17794010.377150163 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0551266 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.46982e+06s, dt:119166s, Cycle: 189 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 7.83e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 2.50e-06 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 8.32e-08 ) ; ( R ) = ( 5.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18189283.331875775 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 18525248.60842841 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 17852219.670575988 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.32666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0798331 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.58899e+06s, dt:108962s, Cycle: 190 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 8.54e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.90e-06 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-04 ) ; ( Rwell ) = ( 1.57e-07 ) ; ( R ) = ( 2.17e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18241540.69014383 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 18577148.429481223 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 17905154.738698512 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.292746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777985 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.69795e+06s, dt:101429s, Cycle: 191 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.55e-07 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 4.95e-07 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18289962.003443226 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 18625217.251734972 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17954215.563862637 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260186 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0703311 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.79938e+06s, dt:101110s, Cycle: 192 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 4.95e-07 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.92e-06 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 6.07e-08 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18337873.628342073 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 18672803.74366999 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 18002995.297686394 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.256076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643202 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.90049e+06s, dt:106892s, Cycle: 193 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 4.58e-07 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 8.71e-08 ) ; ( R ) = ( 8.25e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18388918.363641217 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 18723453.445938323 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 18054839.133496094 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585915 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00074e+07s, dt:119922s, Cycle: 194 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 8.92e-08 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 5.26e-07 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.44e-07 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-06 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 2.71e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18446160.562450435 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 18780191.505812816 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 18112850.588830706 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307366 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668793 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01273e+07s, dt:123595s, Cycle: 195 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 9.42e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 5.33e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.67e-07 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 2.86e-08 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18504792.71153116 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 18838440.841607653 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 18172149.975111227 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659999 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02509e+07s, dt:128490s, Cycle: 196 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 5.33e-07 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18565013.73569213 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 18897946.538999323 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 18232961.6045098 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.311582 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602777 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03794e+07s, dt:141602s, Cycle: 197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 6.55e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 5.17e-07 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.51e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 5.36e-07 ) ; ( R ) = ( 7.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-05 ) ; ( Rwell ) = ( 1.14e-07 ) ; ( R ) = ( 2.47e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18630971.990420613 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 18963542.15779206 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 18299885.72901066 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341492 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607882 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.0521e+07s, dt:155219s, Cycle: 198 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.85e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 8.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 9.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.65e-02 ) ; ( Rwell ) = ( 2.94e-07 ) ; ( R ) = ( 8.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 6.00e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 7.53e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 1.75e-07 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.64e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 6.08e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 6.81e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 7.17e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.90e-05 ) ; ( Rwell ) = ( 1.65e-08 ) ; ( R ) = ( 3.90e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18703751.658490162 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 19035523.23390971 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 18373334.880323384 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.365034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774239 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.06762e+07s, dt:144969s, Cycle: 199 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 6.92e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 8.09e-07 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18771734.78295531 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 19102907.72302304 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 18442140.33973722 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.349088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774721 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.08212e+07s, dt:135338s, Cycle: 200 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 3.78e-08 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18834145.833719302 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19164990.48031982 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 18505412.498237416 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.330253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0732024 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.09565e+07s, dt:131333s, Cycle: 201 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.37e-07 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 2.97e-07 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18894161.258638628 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 19224729.461585402 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 18566245.352304116 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.323945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682303 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.10878e+07s, dt:133584s, Cycle: 202 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.97e-07 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 6.44e-07 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 8.86e-08 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-05 ) ; ( Rwell ) = ( 1.70e-08 ) ; ( R ) = ( 1.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18955400.559826598 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 19285216.834178574 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 18628339.90241917 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.329066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0718764 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.12214e+07s, dt:131239s, Cycle: 203 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 5.62e-07 ) ; ( R ) = ( 1.95e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.81e-02 ) ; ( Rwell ) = ( 2.66e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 1.34e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 4.66e-07 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-05 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 1.59e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19015453.949442945 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 19344486.8971354 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 18689093.70018288 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.317381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692362 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13527e+07s, dt:132200s, Cycle: 204 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 6.58e-07 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 1.77e-08 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19075948.921386205 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 19404301.932235632 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 18750181.081751414 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313232 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064528 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14849e+07s, dt:139469s, Cycle: 205 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 8.28e-07 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 2.73e-07 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19139632.90205272 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 19467480.625971004 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 18814524.606943604 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335552 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736475 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.16243e+07s, dt:134787s, Cycle: 206 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.73e-07 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.13e-06 ) ; ( Rwell ) = ( 7.77e-10 ) ; ( R ) = ( 2.13e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19201767.29521002 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 19528690.729746073 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 18877188.10297039 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.329717 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697335 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.17591e+07s, dt:135129s, Cycle: 207 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 5.41e-07 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-05 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 4.14e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19262955.076106925 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19589143.834852904 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 18938892.467788838 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320741 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618974 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18943e+07s, dt:146429s, Cycle: 208 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 8.43e-07 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-05 ) ; ( Rwell ) = ( 9.03e-08 ) ; ( R ) = ( 3.46e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19328681.90009088 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19654477.272759188 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 19005331.509521212 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.330681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066285 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.20407e+07s, dt:151800s, Cycle: 209 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 9.13e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 4.81e-08 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.57e-06 ) ; ( Rwell ) = ( 4.02e-09 ) ; ( R ) = ( 8.57e-06 ) ; + Last LinSolve(iter,res) = ( 3, 4.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19396424.57342305 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 19721928.021107808 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 19073942.9186941 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.333046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690469 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.21925e+07s, dt:153190s, Cycle: 210 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.28e-09 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.53e-06 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-05 ) ; ( Rwell ) = ( 3.45e-08 ) ; ( R ) = ( 2.80e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19464433.95074377 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 19789215.47862211 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 19142724.871691793 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.336618 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685314 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.23457e+07s, dt:155363s, Cycle: 211 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 8.04e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 4.84e-07 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 3.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19534345.40577785 Pa +wellControls1: Total rate: 56.32837354192298 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls2: BHP (at the specified reference elevation): 19858150.12306143 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 19213455.50249326 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.347908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0890164 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.2501e+07s, dt:131540s, Cycle: 212 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 5.46e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 4.85e-07 ) ; ( R ) = ( 6.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.66e-06 ) ; ( Rwell ) = ( 7.51e-09 ) ; ( R ) = ( 5.66e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19593583.287423227 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 19916461.81570751 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 19273199.34995624 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.287241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755333 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.26326e+07s, dt:124955s, Cycle: 213 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 6.24e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 6.45e-07 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-05 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 4.04e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19649317.979580443 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19971593.338247508 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 19329465.424672 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.26526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637888 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27575e+07s, dt:132812s, Cycle: 214 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 6.34e-07 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.56e-07 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-05 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 1.42e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19708422.612369962 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20030112.90534688 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 19389038.640460264 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281852 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0581549 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28903e+07s, dt:149699s, Cycle: 215 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 6.10e-07 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.86e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 3.77e-07 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-05 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 4.17e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19774466.968264736 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20095654.72862429 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 19455625.34731026 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.321156 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069881 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.304e+07s, dt:149869s, Cycle: 216 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 1.21e-07 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 8.66e-07 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.18e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 3.03e-07 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.71e-05 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 8.71e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19840099.443055514 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 20160548.935479797 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 19521724.407489996 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.314164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.124379 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.31899e+07s, dt:98734.8s, Cycle: 217 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 9.38e-07 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 2.17e-08 ) ; ( R ) = ( 4.77e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.29e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19883388.58241768 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20203182.711746313 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 19565370.31866251 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.212566 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753619 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.32886e+07s, dt:93937.8s, Cycle: 218 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 9.43e-07 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.78e-05 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 7.78e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19924395.03604102 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20243578.011944935 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 19606719.857045762 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.198828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588713 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33826e+07s, dt:105074s, Cycle: 219 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.99e-06 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 2.22e-07 ) ; ( R ) = ( 4.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19970684.56295377 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 20289243.89384724 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 19653297.378481038 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0581421 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34877e+07s, dt:118451s, Cycle: 220 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.23e-07 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 1.39e-06 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 7.25e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 7.00e-07 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20022928.50132058 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 20340721.964891613 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 19705638.298381053 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672255 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36061e+07s, dt:121666s, Cycle: 221 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 9.19e-09 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 1.10e-06 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.89e-05 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 4.89e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20075930.6674722 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 20392993.12304485 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 19758873.935660094 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.259967 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762417 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.37278e+07s, dt:114840s, Cycle: 222 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.52e-06 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 2.69e-08 ) ; ( R ) = ( 5.71e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20125700.05589103 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20442054.52896284 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 19809025.03108489 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.24083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684945 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38426e+07s, dt:116510s, Cycle: 223 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-05 ) ; ( Rwell ) = ( 2.19e-08 ) ; ( R ) = ( 2.78e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20175738.819198485 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20491300.40883416 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 19859396.63476013 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.238192 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600446 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39591e+07s, dt:128714s, Cycle: 224 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.22e-06 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 1.60e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 5.02e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 9.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; ( R ) = ( 1.61e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20231106.935732372 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 20545660.945997328 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 19914929.654497895 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.257823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565796 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.40878e+07s, dt:147576s, Cycle: 225 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.63e-07 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20294801.759453155 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 20608608.724250738 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 19978884.12095094 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303942 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0739788 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.42354e+07s, dt:142188s, Cycle: 226 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 4.32e-07 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.81e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 2.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.82e-05 ) ; ( Rwell ) = ( 6.43e-08 ) ; ( R ) = ( 4.82e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20356568.69642135 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 20669635.08542554 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20041016.14270786 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0795795 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.43776e+07s, dt:130300s, Cycle: 227 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 6.58e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 3.81e-06 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 1.69e-07 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20413296.943946846 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 20725662.20047843 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 20098063.32844915 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0785239 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.45079e+07s, dt:120517s, Cycle: 228 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 1.70e-07 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.37e-06 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20465354.40001312 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 20776918.878762122 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20150287.76876397 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254544 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0741736 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.46284e+07s, dt:115910s, Cycle: 229 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 8.11e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20514655.310026433 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 20825428.325418912 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20199739.845027987 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683976 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47443e+07s, dt:117706s, Cycle: 230 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 1.57e-06 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 7.79e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 7.38e-07 ) ; ( R ) = ( 5.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20563982.95386813 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 20873972.377181333 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20249209.950081754 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.236216 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0620953 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4862e+07s, dt:127289s, Cycle: 231 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.92e-02 ) ; ( Rwell ) = ( 2.06e-06 ) ; ( R ) = ( 7.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.83e-06 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.79e-05 ) ; ( Rwell ) = ( 7.89e-08 ) ; ( R ) = ( 4.79e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20617386.596230593 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 20926965.386034667 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 20303024.340250157 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260201 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600539 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49893e+07s, dt:140608s, Cycle: 232 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-01 ) ; ( Rwell ) = ( 3.58e-06 ) ; ( R ) = ( 4.63e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 1.77e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 8.60e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 4.06e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.79e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 4.53e-07 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 2.10e-07 ) ; ( R ) = ( 5.26e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20676354.6918925 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 20985313.64037178 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20362257.532960534 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.283066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0805362 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.51299e+07s, dt:127785s, Cycle: 233 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.10e-07 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.75e-06 ) ; ( Rwell ) = ( 8.46e-09 ) ; ( R ) = ( 8.75e-06 ) ; + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20730142.755422816 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 21038498.771737054 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20416330.576158196 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.264861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734401 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.52577e+07s, dt:123731s, Cycle: 234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 9.96e-09 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 3.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20782174.751666956 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21089774.701739665 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20468435.261398416 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.256957 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682653 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.53815e+07s, dt:125810s, Cycle: 235 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.15e-09 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 9.27e-08 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.11e-05 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 5.11e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20835112.95254677 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 21141778.136546705 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 20521433.783338293 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.252212 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661996 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55073e+07s, dt:130534s, Cycle: 236 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.31e-06 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 2.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 5.29e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20889872.562139016 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 21195583.6408555 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 20576264.580820214 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.257098 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601055 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56378e+07s, dt:130205s, Cycle: 237 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.15e-06 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.59e-04 ) ; ( Rwell ) = ( 1.48e-07 ) ; ( R ) = ( 3.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20943839.52919437 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 21248640.894672535 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20630153.27084229 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234905 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667786 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5768e+07s, dt:134326s, Cycle: 238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 3.20e-06 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-05 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 2.72e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20999578.29185547 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21303491.2497427 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 20685878.53236884 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672371 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59023e+07s, dt:137956s, Cycle: 239 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 3.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-04 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 1.62e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21056512.70076125 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 21359663.262314547 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 20742857.117337834 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0740844 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.60403e+07s, dt:132791s, Cycle: 240 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; ( R ) = ( 3.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 8.32e-07 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 6.61e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21111167.56470688 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 21413393.615267936 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20797535.81985033 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.246279 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0766686 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.61731e+07s, dt:124861s, Cycle: 241 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 2.46e-06 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 4.85e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21162987.61152248 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 21464373.548951793 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 20849468.108581036 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233678 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0713214 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.62979e+07s, dt:123309s, Cycle: 242 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.20e-06 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-05 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 4.52e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21214390.815099917 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 21515220.53308164 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20901212.349526495 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243963 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0751318 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.64212e+07s, dt:117563s, Cycle: 243 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 2.77e-07 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-05 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 5.94e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21263766.115450047 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 21563572.181429956 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 20950629.055303182 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22475 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769954 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.65388e+07s, dt:110220s, Cycle: 244 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.57e-07 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-05 ) ; ( Rwell ) = ( 4.43e-09 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21309868.617182717 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21608955.31437013 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20996814.830421824 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.213421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675449 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6649e+07s, dt:112859s, Cycle: 245 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 4.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.83e-07 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.22e-05 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 6.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21356630.837906357 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21654902.753383793 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21043653.415964115 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218918 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672487 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.67619e+07s, dt:115896s, Cycle: 246 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.00e-02 ) ; ( Rwell ) = ( 7.23e-07 ) ; ( R ) = ( 9.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.71e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 1.95e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 3.54e-07 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 2.73e-08 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21404381.647704035 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 21701927.590603676 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 21091594.306725085 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.223599 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066836 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.68778e+07s, dt:119497s, Cycle: 247 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 1.95e-06 ) ; ( R ) = ( 9.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 9.88e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.08e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.64e-06 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.53e-05 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 7.53e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21453822.383788466 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 21750286.535045817 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 21141037.223105703 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218152 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0803157 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.69973e+07s, dt:108807s, Cycle: 248 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 6.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.96e-05 ) ; ( Rwell ) = ( 9.63e-09 ) ; ( R ) = ( 7.96e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.90e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21498472.29299286 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 21794056.843867775 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21185722.17947041 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.201247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762465 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.71061e+07s, dt:102697s, Cycle: 249 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 9.63e-09 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.30e-06 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 2.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21540971.010483034 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21835818.649302453 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 21228223.33987763 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195099 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695607 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.72088e+07s, dt:103129s, Cycle: 250 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 5.96e-09 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 7.58e-08 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21583722.882155802 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21877868.74575062 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 21271027.16152917 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195442 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626065 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.73119e+07s, dt:110941s, Cycle: 251 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 7.70e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 6.56e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 2.75e-08 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21629565.595507413 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 21922845.623042718 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21316887.326949526 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.206373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565933 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.74229e+07s, dt:127179s, Cycle: 252 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.27e-06 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21682007.040599212 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21974355.05439386 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 21369394.636904005 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.231338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612759 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.755e+07s, dt:138704s, Cycle: 253 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.20e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.26e-06 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-05 ) ; ( Rwell ) = ( 2.09e-08 ) ; ( R ) = ( 2.37e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21738870.091861606 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22030235.53303721 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 21426316.80989576 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.242689 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068717 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.76887e+07s, dt:140419s, Cycle: 254 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 2.30e-06 ) ; ( R ) = ( 9.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 4.99e-08 ) ; ( R ) = ( 5.89e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21796264.582132213 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 22086705.732589103 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 21483767.53190609 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.242551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0782659 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.78292e+07s, dt:130172s, Cycle: 255 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 2.52e-06 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.28e-06 ) ; ( Rwell ) = ( 8.15e-09 ) ; ( R ) = ( 9.28e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21849529.580101226 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22138871.10106899 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 21537044.467591412 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.226308 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665031 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.79593e+07s, dt:134657s, Cycle: 256 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 8.15e-09 ) ; ( R ) = ( 3.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 2.39e-07 ) ; ( R ) = ( 9.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-06 ) ; ( Rwell ) = ( 3.87e-09 ) ; ( R ) = ( 2.34e-06 ) ; + Last LinSolve(iter,res) = ( 3, 7.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21904109.86851281 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22192412.397868577 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 21591618.60946519 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.224289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578958 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8094e+07s, dt:152202s, Cycle: 257 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 8.97e-07 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.09e-08 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-06 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 2.37e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21965925.460282806 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 22253216.733134568 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 21653449.05435523 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.256266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0543877 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.82462e+07s, dt:178786s, Cycle: 258 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.21e-06 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.45e-08 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-07 ) ; ( Rwell ) = ( 3.75e-10 ) ; ( R ) = ( 5.81e-07 ) ; + Last LinSolve(iter,res) = ( 6, 1.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22039161.01556664 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 22325172.400548257 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 21726554.064316202 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.306681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0846443 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.8425e+07s, dt:156903s, Cycle: 259 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 9.08e-07 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22103477.060700525 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22388307.912786923 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026233 sm3/s +wellControls3: BHP (at the specified reference elevation): 21790748.972521435 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.270534 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0822711 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.85819e+07s, dt:140484s, Cycle: 260 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 9.03e-07 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.27e-07 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-06 ) ; ( Rwell ) = ( 5.19e-09 ) ; ( R ) = ( 2.46e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22160662.792533003 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22444583.821067393 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21847828.152389187 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.236317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753746 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.87224e+07s, dt:133644s, Cycle: 261 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 3.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 8.72e-07 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 4.35e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 4.58e-07 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.01e-06 ) ; ( Rwell ) = ( 2.34e-08 ) ; ( R ) = ( 8.01e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22214558.349627066 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22497516.27931259 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 21901561.863619767 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.225488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688334 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8856e+07s, dt:135145s, Cycle: 262 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 1.21e-06 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.30e-06 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 6.30e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22269311.249822434 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22551109.905369833 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 21956112.014812134 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.230676 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623024 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.89911e+07s, dt:145837s, Cycle: 263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.64e-06 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.12e-08 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-05 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 1.06e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22328661.46402825 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 22609495.072320726 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 22015410.13753575 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662131 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9137e+07s, dt:151293s, Cycle: 264 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.06e-07 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.96e-05 ) ; ( Rwell ) = ( 8.14e-08 ) ; ( R ) = ( 7.96e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22390429.61198555 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 22670140.013636433 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 22077200.38219628 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067224 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.92883e+07s, dt:155402s, Cycle: 265 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 8.24e-08 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.87e-02 ) ; ( Rwell ) = ( 6.65e-07 ) ; ( R ) = ( 9.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-05 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 3.12e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22454123.23937908 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22732601.448207352 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 22140918.652570743 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0616677 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.94437e+07s, dt:168797s, Cycle: 266 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 1.66e-06 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 8.29e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 9.98e-07 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.07e-05 ) ; ( Rwell ) = ( 4.89e-08 ) ; ( R ) = ( 5.07e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22522673.9499703 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22799889.816377126 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 22209376.448748637 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.297387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689835 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.96125e+07s, dt:170447s, Cycle: 267 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.00e-06 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.00e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 7.14e-07 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 8.58e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 9.30e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.29e-07 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-06 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 2.51e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22591675.391449124 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 22867477.504578207 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 22278199.171062484 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.306863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682279 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.97829e+07s, dt:173373s, Cycle: 268 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 8.64e-07 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 9.02e-08 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22661517.61787745 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 22936098.328853052 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 22347973.075987082 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.305347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066993 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.99563e+07s, dt:178484s, Cycle: 269 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 9.11e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 8.98e-07 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-06 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 3.10e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22733081.97068935 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 23006380.113934465 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 22419395.47020832 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.298793 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0742321 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.01348e+07s, dt:171569s, Cycle: 270 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 8.99e-07 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 4.50e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.42e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.32e-05 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 9.32e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22801519.024395097 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 23073614.80905719 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 22487725.84254246 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0784129 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.03063e+07s, dt:158842s, Cycle: 271 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 1.82e-06 ) ; ( R ) = ( 7.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 9.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 9.64e-07 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-04 ) ; ( Rwell ) = ( 1.36e-08 ) ; ( R ) = ( 3.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22865160.460247237 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 23135954.120645467 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 22551301.685022276 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281459 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691796 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.04652e+07s, dt:160093s, Cycle: 272 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.31e-06 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 4.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22929637.559764873 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 23199167.981954303 Pa +wellControls2: Total rate: 56.328373541922936 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026258 sm3/s +wellControls3: BHP (at the specified reference elevation): 22615701.44628298 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026284 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575491 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.06253e+07s, dt:181631s, Cycle: 273 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.35e-06 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 7.55e-08 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.66e-06 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 5.66e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23003412.68185511 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 23271494.946664184 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 22689379.056866232 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281702 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641397 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.08069e+07s, dt:192367s, Cycle: 274 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 3.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 1.46e-06 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 7.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.75e-07 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-04 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 3.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23081429.37223441 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 23348154.576610062 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 22767276.519564193 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.301915 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0759639 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.09993e+07s, dt:182028s, Cycle: 275 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23154833.71199422 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 23420122.044918466 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 22840531.388242908 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.290129 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0746577 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.11813e+07s, dt:174297s, Cycle: 276 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-04 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 2.27e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23224766.968730766 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 23488720.328664377 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 22910335.394779973 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.283125 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695815 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.13556e+07s, dt:174994s, Cycle: 277 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23294989.388284676 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 23557541.17590537 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 22980400.127277236 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.290119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.15306e+07s, dt:185717s, Cycle: 278 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.91e-06 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-06 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 1.53e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.79e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23369865.448512975 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 23631075.061333522 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23055173.045771215 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.310245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679098 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17163e+07s, dt:189489s, Cycle: 279 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.79e-05 ) ; ( Rwell ) = ( 1.34e-08 ) ; ( R ) = ( 6.79e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23446179.4808966 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 23706066.466195133 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 23131378.484341513 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715947 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.19058e+07s, dt:186654s, Cycle: 280 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.46e-06 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.67e-05 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 7.67e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23521346.84692883 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 23779852.45856758 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 23206436.841334134 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.291839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654538 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.20925e+07s, dt:195101s, Cycle: 281 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.99e-06 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 3.83e-08 ) ; ( R ) = ( 8.35e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23599867.901919246 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 23856878.626453966 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 23284854.26154114 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.296182 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623441 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.22876e+07s, dt:210446s, Cycle: 282 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.37e-06 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 5.13e-08 ) ; ( R ) = ( 5.92e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23684336.240832593 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 23939740.68955859 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23369250.63001859 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.322012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588384 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.2498e+07s, dt:235477s, Cycle: 283 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 2.40e-06 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e-04 ) ; ( Rwell ) = ( 9.42e-08 ) ; ( R ) = ( 2.23e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23778605.830452695 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 24032330.363923945 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 23463422.0438841 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.362643 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.074912 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.27335e+07s, dt:224953s, Cycle: 284 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 9.33e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.44e-06 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.15e-05 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 7.15e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23868915.800627496 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 24120866.20360878 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23553517.30298772 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728828 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.29584e+07s, dt:218942s, Cycle: 285 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 3.21e-06 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.37e-05 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 9.37e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23956482.030712854 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 24206888.16226381 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23640923.63023805 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734887 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.31774e+07s, dt:211902s, Cycle: 286 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.13e-02 ) ; ( Rwell ) = ( 3.12e-06 ) ; ( R ) = ( 8.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.57e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.28e-03 ) ; ( Rwell ) = ( 1.69e-06 ) ; ( R ) = ( 7.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24041381.82761936 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 24290225.366899185 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 23725816.487186663 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.325697 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658704 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.33893e+07s, dt:220577s, Cycle: 287 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.30e-06 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-04 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 2.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24129618.816039428 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 24376855.341496397 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 23813968.095953505 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0819526 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.36099e+07s, dt:198034s, Cycle: 288 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 4.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.00e-02 ) ; ( Rwell ) = ( 1.01e-06 ) ; ( R ) = ( 8.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.62e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.90e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 7.58e-07 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.16e-05 ) ; ( Rwell ) = ( 7.67e-08 ) ; ( R ) = ( 7.16e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24208571.131074257 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 24454456.551856846 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 23892872.820454773 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.292021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0834699 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.38079e+07s, dt:175518s, Cycle: 289 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.66e-06 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 8.56e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.01e-06 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-05 ) ; ( Rwell ) = ( 4.48e-09 ) ; ( R ) = ( 2.54e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24278283.530943953 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 24522890.91413548 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 23962468.07770354 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.076767 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.39834e+07s, dt:164891s, Cycle: 290 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-05 ) ; ( Rwell ) = ( 8.02e-09 ) ; ( R ) = ( 4.54e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24343756.95501032 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 24587290.789483752 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 24027876.331143245 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697904 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.41483e+07s, dt:165221s, Cycle: 291 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 8.02e-09 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.93e-06 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.76e-08 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-06 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 2.94e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.49e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24409753.72290651 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 24652198.144896768 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 24093918.80850075 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255659 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630505 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.43135e+07s, dt:176931s, Cycle: 292 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-04 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 1.35e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24480228.36544884 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 24721489.219652306 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 24164382.03190127 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274299 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612228 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.44905e+07s, dt:193070s, Cycle: 293 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 2.22e-06 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 5.55e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 4.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 8.84e-07 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24556701.59796472 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 24796535.32743928 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 24240679.999209322 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.280453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657923 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.46835e+07s, dt:201130s, Cycle: 294 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.20e-06 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.21e-07 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-06 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.03e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.19e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24636041.15541591 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 24874522.55095674 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 24319905.47843412 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.288183 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637061 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.48847e+07s, dt:213955s, Cycle: 295 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 2.51e-06 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-06 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 5.72e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24720722.748516906 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 24957793.305605166 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 24404504.231086858 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641457 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.50986e+07s, dt:226588s, Cycle: 296 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 2.52e-06 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.26e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24810511.913981445 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 25045955.867117595 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 24494173.83801988 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.328069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755754 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.53252e+07s, dt:215164s, Cycle: 297 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 9.58e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 9.36e-07 ) ; ( R ) = ( 8.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24895397.972284768 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 25129421.350241795 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 24578968.505436193 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762618 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.55404e+07s, dt:203054s, Cycle: 298 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.58e-06 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-06 ) ; ( Rwell ) = ( 6.83e-10 ) ; ( R ) = ( 1.01e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.36e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 24974866.863420922 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 25207598.952093378 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 24658346.974658012 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0729699 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.57434e+07s, dt:197469s, Cycle: 299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.47e-06 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 8.90e-08 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25051900.198813986 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 25283359.404524088 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 24735304.21145166 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.276684 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688348 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.59409e+07s, dt:199685s, Cycle: 300 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.25e-06 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-04 ) ; ( Rwell ) = ( 8.70e-08 ) ; ( R ) = ( 1.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25129746.89184453 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 25360006.348698605 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 24813103.108245265 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.285204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0729207 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.61406e+07s, dt:194280s, Cycle: 301 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 8.77e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.14e-06 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 7.80e-08 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.16e-06 ) ; ( Rwell ) = ( 8.13e-09 ) ; ( R ) = ( 6.16e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25205300.059666596 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 25434407.105860915 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 24888601.73918165 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.272574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734365 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.63348e+07s, dt:188123s, Cycle: 302 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 8.92e-09 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 8.51e-07 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-04 ) ; ( Rwell ) = ( 1.47e-07 ) ; ( R ) = ( 4.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 1.00e-02 ) ; +wellControls1: BHP (at the specified reference elevation): 25278700.59993593 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 25506588.37425939 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 24961963.03076382 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255583 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636535 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.6523e+07s, dt:200226s, Cycle: 303 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.47e-07 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.46e-06 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 7.59e-08 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.01e-06 ) ; ( Rwell ) = ( 4.53e-09 ) ; ( R ) = ( 8.01e-06 ) ; + Last LinSolve(iter,res) = ( 3, 7.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25357193.60404824 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 25583699.11003776 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 25040366.90709874 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.273639 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0616258 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.67232e+07s, dt:217578s, Cycle: 304 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 5.32e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.25e-06 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 7.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25442643.655040745 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 25667783.859353952 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 25125765.282820147 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0768044 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.69408e+07s, dt:204337s, Cycle: 305 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.59e-06 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.96e-06 ) ; ( Rwell ) = ( 1.85e-09 ) ; ( R ) = ( 5.96e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25522764.06052871 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 25746720.065137804 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 25205847.758921195 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279364 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.075817 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.71451e+07s, dt:193611s, Cycle: 306 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 9.31e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 3.25e-07 ) ; ( R ) = ( 8.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.43e-05 ) ; ( Rwell ) = ( 4.69e-08 ) ; ( R ) = ( 6.43e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25598733.546596408 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 25821528.660724163 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 25281782.62760894 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.267724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0763165 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.73387e+07s, dt:182624s, Cycle: 307 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.63e-06 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-05 ) ; ( Rwell ) = ( 2.21e-08 ) ; ( R ) = ( 3.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25670465.138156008 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 25892038.824314874 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 25353441.033419907 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721886 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.75213e+07s, dt:178896s, Cycle: 308 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 4.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.65e-05 ) ; ( Rwell ) = ( 3.69e-08 ) ; ( R ) = ( 4.65e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25740499.131639197 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 25960897.257830024 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 25423397.071510762 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0744067 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.77002e+07s, dt:171690s, Cycle: 309 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 8.61e-07 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.36e-05 ) ; ( Rwell ) = ( 3.72e-08 ) ; ( R ) = ( 7.36e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25807813.060194273 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 26027140.514475442 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 25490716.422508862 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.24007 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0798144 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.78719e+07s, dt:157014s, Cycle: 310 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.83e-02 ) ; ( Rwell ) = ( 1.99e-06 ) ; ( R ) = ( 8.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.02e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.04e-05 ) ; ( Rwell ) = ( 5.13e-08 ) ; ( R ) = ( 6.04e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25869427.674094472 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 26087720.53402325 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 25552349.276324 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.216735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0743325 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.80289e+07s, dt:150792s, Cycle: 311 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 2.00e-06 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 7.77e-09 ) ; ( R ) = ( 8.06e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25928400.994996503 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26145655.620013602 Pa +wellControls2: Total rate: 56.32837354192293 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270262066 sm3/s +wellControls3: BHP (at the specified reference elevation): 25611242.947819926 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.203705 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626428 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.81797e+07s, dt:162154s, Cycle: 312 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 7.00e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.12e-06 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.73e-05 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 8.73e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25991512.82743911 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 26207790.02591913 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 25674303.39153525 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218328 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594739 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.83419e+07s, dt:180220s, Cycle: 313 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-06 ) ; ( Rwell ) = ( 4.32e-10 ) ; ( R ) = ( 2.23e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26061314.64225273 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26276551.251257308 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 25744059.325136885 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684205 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.85221e+07s, dt:182973s, Cycle: 314 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.80e-08 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.63e-06 ) ; ( Rwell ) = ( 7.25e-09 ) ; ( R ) = ( 9.63e-06 ) ; + Last LinSolve(iter,res) = ( 2, 9.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26132039.86237541 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 26346269.40526798 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 25814735.14317776 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.247227 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0569878 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.87051e+07s, dt:208855s, Cycle: 315 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 7.96e-09 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 6.62e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 8.67e-07 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-06 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 9.11e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26213095.335310362 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 26426115.020685732 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 25895724.12480854 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.282822 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.117539 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.89139e+07s, dt:143765s, Cycle: 316 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.54e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.64e-06 ) ; ( Rwell ) = ( 3.22e-09 ) ; ( R ) = ( 8.64e-06 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26268835.476059105 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 26481025.2174237 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 25951446.174146563 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.187049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0905749 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.90577e+07s, dt:120210s, Cycle: 317 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 2.32e-07 ) ; ( R ) = ( 6.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-05 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 5.10e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26315301.54173911 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26526799.727356557 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 25997926.088479128 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.158692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769853 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.91779e+07s, dt:112712s, Cycle: 318 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.02e-03 ) ; ( Rwell ) = ( 2.52e-07 ) ; ( R ) = ( 7.02e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.77e-05 ) ; ( Rwell ) = ( 6.44e-09 ) ; ( R ) = ( 5.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26359006.5369528 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26569827.85799728 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 26041659.18040768 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.151818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671976 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.92906e+07s, dt:115802s, Cycle: 319 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 3.90e-07 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-05 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 2.30e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26404280.316187005 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26614389.968132693 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 26086956.923694342 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.151595 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557441 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.94064e+07s, dt:133995s, Cycle: 320 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.03e-07 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-05 ) ; ( Rwell ) = ( 7.96e-08 ) ; ( R ) = ( 2.35e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26456519.446545467 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 26665838.293854617 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26139208.9733233 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.173363 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0491219 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.95404e+07s, dt:167251s, Cycle: 321 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 6.56e-07 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.31e-08 ) ; ( R ) = ( 8.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26521380.55629127 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 26729665.331853285 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 26204053.658043247 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.214615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774019 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.97077e+07s, dt:156237s, Cycle: 322 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 5.13e-07 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 7.12e-08 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.03e-06 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 8.03e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26581764.028370716 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26789160.872423284 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 26264430.536942843 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.199103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.057598 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.98639e+07s, dt:177162s, Cycle: 323 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.66e-07 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-06 ) ; ( Rwell ) = ( 5.68e-11 ) ; ( R ) = ( 1.58e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26650705.435604762 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26857028.630370274 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 26333360.160502605 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.228081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.111066 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.00411e+07s, dt:127354s, Cycle: 324 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 9.71e-10 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.15e-07 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; ( R ) = ( 5.94e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26700380.961331602 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26906080.93644759 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26383035.94574738 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.164188 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684034 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.01684e+07s, dt:129320s, Cycle: 325 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-06 ) ; ( Rwell ) = ( 1.74e-10 ) ; ( R ) = ( 1.69e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26751032.161167156 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26956036.217549007 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 26433698.058140904 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.166981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0524013 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.02977e+07s, dt:155359s, Cycle: 326 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 9.70e-10 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 4.52e-07 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 2.25e-08 ) ; ( R ) = ( 9.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26811832.901997883 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27015968.911869098 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 26494541.941107728 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.199526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.101408 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.04531e+07s, dt:119588s, Cycle: 327 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 3.41e-07 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-05 ) ; ( Rwell ) = ( 6.91e-09 ) ; ( R ) = ( 3.31e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26858575.910603616 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27062045.68369454 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 26541313.58754016 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.154389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0743892 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.05727e+07s, dt:114790s, Cycle: 328 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 6.91e-09 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 4.38e-07 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.72e-05 ) ; ( Rwell ) = ( 2.35e-08 ) ; ( R ) = ( 5.72e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26903257.791840333 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27106083.556338467 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 26586000.239712738 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.148834 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621201 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.06875e+07s, dt:124103s, Cycle: 329 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.39e-07 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 1.02e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26951504.856022608 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27153636.776272167 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 26634258.19681451 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.16237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0785337 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.08116e+07s, dt:114775s, Cycle: 330 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 4.70e-07 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-04 ) ; ( Rwell ) = ( 4.37e-08 ) ; ( R ) = ( 1.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26995944.954055544 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 27197461.28466131 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26678711.317049228 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.150617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0811316 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.09264e+07s, dt:103773s, Cycle: 331 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 3.46e-07 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 7.43e-08 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27036105.00922547 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27237074.13515038 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 26718890.800886977 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.136259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0711568 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.10301e+07s, dt:102643s, Cycle: 332 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 7.49e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.75e-07 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27075891.161322135 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 27276263.14470493 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 26758680.831821807 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.132538 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638391 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.11328e+07s, dt:109041s, Cycle: 333 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 3.11e-07 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-05 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 4.66e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27118094.6393445 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 27317872.46024215 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26800911.49818272 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.139099 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0551158 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.12418e+07s, dt:127051s, Cycle: 334 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 9.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.50e-05 ) ; ( Rwell ) = ( 4.30e-09 ) ; ( R ) = ( 6.50e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27167113.806474622 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 27366228.516251996 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 26849947.147123694 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.160511 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0605758 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.13689e+07s, dt:139578s, Cycle: 335 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 1.89e-07 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.66e-04 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 3.66e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27220920.982754134 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 27419302.069424786 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26903764.189188045 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.176579 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0560994 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.15084e+07s, dt:27553.4s, Cycle: 336 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ; ( Rwell ) = ( 3.26e-07 ) ; ( R ) = ( 1.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27231485.990047652 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27429799.143916663 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26914426.30185358 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0366509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0106359 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.1536e+07s, dt:55106.9s, Cycle: 337 +compflowStatistics, Reservoir: Pressure (min, average, max): 2.80948e+07, 2.99421e+07, 3.12538e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 1.55836e+07, 1.87425e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.66516e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 19105.6, 6.66325e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 1.3012e+07, 6.51497e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 3.678e+06, 1.95506e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 9.334e+06, 4.55991e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.3012e+07, 6.51497e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 1.3012e+07, 0 }, { 1.5239e+07, 6.51342e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 2.76478e+07, 2.89944e+07, 2.98486e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 1.51365e+07, 1.73373e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.30522e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 32957.1, 1.30193e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 2.22162e+07, 1.27238e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 6.26215e+06, 3.82691e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 1.5954e+07, 8.89688e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 222587, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 2.19936e+07, 1.27238e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 2.22162e+07, 0 }, { 1.71021e+07, 1.27063e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 2.53214e+07, 2.70209e+07, 2.93395e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 1.28101e+07, 1.68282e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.32444e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 7.22338e+06, 1.2522e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 4.51094e+09, 1.22328e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 5.22525e+08, 3.88342e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 3.98842e+09, 8.34943e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 5.98006e+06, 0 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 4.50496e+09, 1.22328e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 4.51094e+09, 0 }, { 7.22016e+08, 1.21591e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 2.89468e+07, 3.19674e+07, 3.35544e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 1.64355e+07, 2.10431e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.1034e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 0, 1.1034e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 0, 1.08036e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 0, 3.24108e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 0, 7.56253e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 0, 1.08036e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 0, 0 }, { 872133, 1.08035e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 2.56026e+07, 3.21242e+07, 3.43215e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 1.30913e+07, 2.18102e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.37279e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 0, 6.37279e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 0, 6.24042e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 0, 1.87213e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 0, 4.36829e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 0, 6.24042e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 0, 0 }, { 1.05563e+06, 6.24031e+10 } } kg +compflowStatistics: Max phase CFL number: 0.721008 +compflowStatistics: Max component CFL number: 1.15538 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 6.85e-07 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27252686.916117527 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27450836.07294756 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26935804.208137162 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0702061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0218585 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.15911e+07s, dt:101765s, Cycle: 338 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 6.85e-07 ) ; ( R ) = ( 2.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 1.87e-07 ) ; ( R ) = ( 9.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 8.56e-09 ) ; ( R ) = ( 7.14e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27292249.75623648 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 27489692.20786002 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 26975165.614469677 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.12949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0395985 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.16929e+07s, dt:143238s, Cycle: 339 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 7.94e-09 ) ; ( R ) = ( 3.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 6.65e-07 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.49e-05 ) ; ( Rwell ) = ( 6.78e-09 ) ; ( R ) = ( 4.49e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27347828.021346074 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 27544558.984344654 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 27030829.22093828 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.183932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0571339 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.18361e+07s, dt:163241s, Cycle: 340 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 6.78e-09 ) ; ( R ) = ( 3.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 8.88e-07 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-04 ) ; ( Rwell ) = ( 1.28e-07 ) ; ( R ) = ( 2.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.82e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27411126.838983413 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 27606977.186915647 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 27094194.51141898 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.206719 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728846 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.19994e+07s, dt:158876s, Cycle: 341 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.38e-06 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.27e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; ( R ) = ( 3.27e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27472806.320469126 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27667748.505417176 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 27155894.875342 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.203614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0836309 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.21582e+07s, dt:140621s, Cycle: 342 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 6.63e-09 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 2.06e-06 ) ; ( R ) = ( 9.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.82e-05 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 8.82e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27527481.40944904 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27721626.796346016 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 27210580.6455129 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.181701 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0786582 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.22988e+07s, dt:129909s, Cycle: 343 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 6.98e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.51e-05 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 5.51e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27578030.955809318 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27771529.10729304 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 27261147.05613403 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.16864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688339 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.24288e+07s, dt:131368s, Cycle: 344 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 5.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-05 ) ; ( Rwell ) = ( 6.81e-09 ) ; ( R ) = ( 1.24e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27629270.84813136 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 27822142.533044215 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 27312422.94308107 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.170686 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059772 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.25601e+07s, dt:145545s, Cycle: 345 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 7.21e-09 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.12e-06 ) ; ( R ) = ( 6.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.04e-06 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.62e-06 ) ; ( Rwell ) = ( 4.16e-09 ) ; ( R ) = ( 2.62e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27686115.060085054 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27878283.513974134 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 27369326.59958768 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.187415 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0549244 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.27057e+07s, dt:169945s, Cycle: 346 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.11e-06 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-05 ) ; ( Rwell ) = ( 6.31e-09 ) ; ( R ) = ( 2.78e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27752201.305803895 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 27943542.802045852 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 27435489.515934303 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.216392 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0558077 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.28756e+07s, dt:196506s, Cycle: 347 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.79e-06 ) ; ( R ) = ( 4.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.39e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.86e-07 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 2.16e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27828273.540137008 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 28018658.41666545 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 27511646.8693077 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0834978 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.30721e+07s, dt:174123s, Cycle: 348 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-06 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 1.61e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27895411.41380568 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 28084999.92725561 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 27578855.991297334 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.221108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621478 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.32462e+07s, dt:188196s, Cycle: 349 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 5.90e-07 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 2.95e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.66e-07 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.68e-05 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 2.68e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27967978.083065517 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 28156728.026708294 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 27651511.865231685 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234776 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673855 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.34344e+07s, dt:193002s, Cycle: 350 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.34e-07 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-06 ) ; ( Rwell ) = ( 5.88e-11 ) ; ( R ) = ( 1.38e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28042532.13075057 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 28230414.367957205 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 27726157.338561945 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.235449 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0841784 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.36274e+07s, dt:170041s, Cycle: 351 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 8.55e-10 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 8.31e-07 ) ; ( R ) = ( 7.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-05 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 3.91e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28108194.41311428 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 28295285.20546803 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 27791934.169339705 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.207275 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0848234 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.37975e+07s, dt:149005s, Cycle: 352 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 2.20e-07 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.72e-05 ) ; ( Rwell ) = ( 7.13e-09 ) ; ( R ) = ( 4.72e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28165790.755123533 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 28352196.44946675 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 27849595.017645337 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.18187 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0779875 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.39465e+07s, dt:138472s, Cycle: 353 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 7.13e-09 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.48e-07 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.10e-03 ) ; ( Rwell ) = ( 5.07e-08 ) ; ( R ) = ( 8.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 2, 7.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28219202.081098642 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 28404954.94938218 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 27903083.078421615 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.167639 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0709891 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.4085e+07s, dt:137179s, Cycle: 354 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.39e-07 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 1.93e-08 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28272184.21507093 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 28457311.682359047 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 27956159.721376173 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.165229 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064045 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.42221e+07s, dt:145427s, Cycle: 355 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.26e-06 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-05 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 3.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28328330.816919852 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 28512803.835099906 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 28012295.44862657 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.175391 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0567924 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.43676e+07s, dt:166352s, Cycle: 356 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 8.81e-07 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 4.39e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 4.05e-07 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.85e-06 ) ; ( Rwell ) = ( 3.61e-09 ) ; ( R ) = ( 9.85e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28392565.483306825 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 28576255.669904955 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 28076532.77107025 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.201203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0724301 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.45339e+07s, dt:162589s, Cycle: 357 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 2.22e-06 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28455409.08631739 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 28638418.66348689 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 28139417.905586448 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.197891 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696778 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.46965e+07s, dt:163090s, Cycle: 358 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.13e-07 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.29e-06 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.74e-05 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 6.74e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28518567.050439082 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls2: BHP (at the specified reference elevation): 28700850.81169564 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 28202543.539361525 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.200637 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061411 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.48596e+07s, dt:177619s, Cycle: 359 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 6.43e-07 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-04 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 2.78e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28587468.489944406 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 28768997.590675335 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 28271478.573426183 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.220142 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0738213 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.50372e+07s, dt:171382s, Cycle: 360 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 8.40e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-04 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 1.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28653857.30702019 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 28834678.29551118 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 28337916.90263459 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.210809 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0862475 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.52086e+07s, dt:148416s, Cycle: 361 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.54e-06 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 8.06e-09 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28711365.546282034 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 28891602.770297438 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 28395520.363251504 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.180316 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0796094 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.5357e+07s, dt:135972s, Cycle: 362 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.20e-03 ) ; ( Rwell ) = ( 9.59e-07 ) ; ( R ) = ( 9.20e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28764107.874173604 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 28943845.99283859 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 28448347.24457387 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.163303 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715219 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.5493e+07s, dt:134030s, Cycle: 363 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.11e-03 ) ; ( Rwell ) = ( 7.12e-07 ) ; ( R ) = ( 9.11e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-04 ) ; ( Rwell ) = ( 7.66e-08 ) ; ( R ) = ( 1.61e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28816057.067894522 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 28995243.34297908 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 28500320.996890377 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.159316 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636248 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.5627e+07s, dt:142693s, Cycle: 364 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 7.71e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; ( R ) = ( 1.80e-04 ) ; + Last LinSolve(iter,res) = ( 7, 1.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28871221.19619697 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 29049783.556127153 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 28555503.634535264 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.169537 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566291 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.57697e+07s, dt:163516s, Cycle: 365 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 5.62e-07 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.62e-05 ) ; ( Rwell ) = ( 7.71e-09 ) ; ( R ) = ( 5.62e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28934562.273928702 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 29112406.85159906 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 28618893.330697715 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195397 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696588 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.59332e+07s, dt:164049s, Cycle: 366 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 8.03e-09 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 7.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 7.37e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 8.21e-07 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.33e-04 ) ; ( Rwell ) = ( 4.68e-08 ) ; ( R ) = ( 3.33e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 28997983.829622112 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 29175184.90785636 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 28682401.41414317 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.196414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0717515 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.60973e+07s, dt:161357s, Cycle: 367 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.55e-06 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.61e-05 ) ; ( Rwell ) = ( 6.77e-08 ) ; ( R ) = ( 9.61e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29060360.427378047 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 29236865.99966171 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 28744809.819352992 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.19342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688622 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.62586e+07s, dt:163125s, Cycle: 368 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 6.71e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.52e-06 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 2.39e-08 ) ; ( R ) = ( 5.88e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29123208.427053355 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls2: BHP (at the specified reference elevation): 29299061.479348347 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 28807741.64807476 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195925 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645248 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.64218e+07s, dt:172099s, Cycle: 369 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-04 ) ; ( Rwell ) = ( 3.22e-08 ) ; ( R ) = ( 1.22e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29189532.71888872 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 29364686.63598346 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 28874149.518906694 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.209609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0747396 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.65939e+07s, dt:164666s, Cycle: 370 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 7.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 8.05e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 8.23e-07 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 8.14e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.04e-07 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.53e-06 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 4.53e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29252960.87099754 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 29427436.675226547 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 28937670.896950632 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.202886 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0776678 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.67585e+07s, dt:153460s, Cycle: 371 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-05 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 3.45e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29312265.974714927 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 29486092.59158086 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 28997057.423822712 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.190497 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715414 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.6912e+07s, dt:151239s, Cycle: 372 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.77e-03 ) ; ( Rwell ) = ( 3.76e-07 ) ; ( R ) = ( 9.77e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-05 ) ; ( Rwell ) = ( 8.55e-09 ) ; ( R ) = ( 2.31e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29370829.83058203 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 29544030.138865292 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 29055674.86594174 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.187038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642553 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.70632e+07s, dt:159993s, Cycle: 373 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 8.55e-09 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.79e-07 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 1.17e-07 ) ; ( R ) = ( 2.10e-04 ) ; + Last LinSolve(iter,res) = ( 3, 4.39e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29432501.637889937 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 29605088.499144897 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 29117389.993895207 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.193818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0569847 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.72232e+07s, dt:182631s, Cycle: 374 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.65e-02 ) ; ( Rwell ) = ( 1.52e-07 ) ; ( R ) = ( 9.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 5.24e-08 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.99e-05 ) ; ( Rwell ) = ( 6.40e-08 ) ; ( R ) = ( 3.99e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29502752.1352346 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 29674746.929959927 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 29187774.78369078 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.214144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646675 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.74058e+07s, dt:192402s, Cycle: 375 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 6.34e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.42e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 2.46e-08 ) ; ( R ) = ( 5.83e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29576508.897723313 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 29747919.02923389 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 29261662.430660687 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.227602 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0733369 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.75982e+07s, dt:186476s, Cycle: 376 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 2.64e-07 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.51e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 5.01e-07 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.79e-04 ) ; ( Rwell ) = ( 2.26e-09 ) ; ( R ) = ( 2.79e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29648034.706770174 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 29818813.631254766 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 29333289.435415164 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.21781 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0761945 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.77847e+07s, dt:176088s, Cycle: 377 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.81e-06 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-04 ) ; ( Rwell ) = ( 8.94e-08 ) ; ( R ) = ( 3.08e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29715280.76858463 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 29885705.697097454 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 29400904.673315685 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.205459 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0729256 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.79608e+07s, dt:171314s, Cycle: 378 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 8.98e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.90e-07 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-04 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 2.38e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29780726.80066546 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 29950901.490597703 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 29466845.561910916 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.199996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678655 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.81321e+07s, dt:174869s, Cycle: 379 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.07e-08 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 6.82e-09 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29847465.144287497 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 30017356.699014667 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 29534058.107305106 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.206177 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673552 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.8307e+07s, dt:179388s, Cycle: 380 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 6.29e-09 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 4.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.54e-06 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 8.54e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29915961.883314967 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 30085613.741305724 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 29603040.02013465 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.213858 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.085875 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.84864e+07s, dt:155828s, Cycle: 381 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 2.67e-07 ) ; ( R ) = ( 4.68e-04 ) ; + Last LinSolve(iter,res) = ( 2, 7.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 29975384.25003987 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 30144952.99792941 Pa +wellControls2: Total rate: 56.32837354192298 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026592 sm3/s +wellControls3: BHP (at the specified reference elevation): 29662915.137388475 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.183944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737353 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.86422e+07s, dt:150475s, Cycle: 382 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.67e-07 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.23e-05 ) ; ( Rwell ) = ( 5.64e-08 ) ; ( R ) = ( 7.23e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30032722.767394442 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 30201997.14829278 Pa +wellControls2: Total rate: 56.32837354192298 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270266696 sm3/s +wellControls3: BHP (at the specified reference elevation): 29720581.279843457 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.173718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0634811 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.87927e+07s, dt:160436s, Cycle: 383 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 7.52e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 2.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.45e-08 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.26e-07 ) ; ( Rwell ) = ( 3.21e-10 ) ; ( R ) = ( 9.26e-07 ) ; + Last LinSolve(iter,res) = ( 4, 2.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30093917.53696643 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 30262903.310148995 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 29782150.6083104 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.181691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0635956 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.89531e+07s, dt:170857s, Cycle: 384 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 7.21e-10 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 1.71e-06 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-04 ) ; ( Rwell ) = ( 5.60e-08 ) ; ( R ) = ( 2.47e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30158952.154971007 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 30327729.32742422 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 29847603.89258568 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.191896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0904613 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.9124e+07s, dt:142992s, Cycle: 385 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.31e-06 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.27e-06 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 6.27e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30213606.384642232 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 30382198.18219356 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 29902595.2730544 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.163281 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0851104 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.9267e+07s, dt:125003s, Cycle: 386 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 7.88e-07 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.94e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 4.20e-07 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 3.13e-08 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30261479.102983963 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 30429793.234995916 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 29950677.05159303 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.140978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708398 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.9392e+07s, dt:124011s, Cycle: 387 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 7.54e-07 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30308909.337563362 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 30477016.071814917 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 29998426.774244566 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.140383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621073 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.9516e+07s, dt:134091s, Cycle: 388 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 5.28e-07 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.62e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; ( R ) = ( 2.62e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30360149.015133716 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 30528051.876980405 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 30049976.868739847 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.153223 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690175 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.96501e+07s, dt:135357s, Cycle: 389 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 8.17e-09 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.23e-07 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30411857.497029122 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 30579598.106157478 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 30102021.839925718 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.156101 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706965 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.97854e+07s, dt:134465s, Cycle: 390 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 7.10e-09 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 5.68e-07 ) ; ( R ) = ( 9.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.77e-05 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 5.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30463288.07374959 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 30630879.973518696 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 30153792.564783018 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.155736 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0635961 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.99199e+07s, dt:143199s, Cycle: 391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 6.47e-07 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.51e-08 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30518226.027167417 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 30685573.284090053 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 30209056.73980417 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.165952 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0812259 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.00631e+07s, dt:129368s, Cycle: 392 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; ( R ) = ( 4.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 8.92e-07 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.93e-04 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 3.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30567777.83850678 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 30734861.785899885 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 30258839.45817235 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.149457 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.062722 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.01925e+07s, dt:139003s, Cycle: 393 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 5.66e-07 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 3.29e-10 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30620900.33917509 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 30787691.554604076 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 30312205.968732495 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.159472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064317 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.03315e+07s, dt:146956s, Cycle: 394 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 8.15e-10 ) ; ( R ) = ( 4.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 5.71e-07 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 9.13e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30677123.303069454 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 30843707.249887902 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 30368748.700972002 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.167911 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0742034 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.04784e+07s, dt:141300s, Cycle: 395 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 7.80e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 9.70e-07 ) ; ( R ) = ( 4.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 4.87e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.18e-05 ) ; ( Rwell ) = ( 3.24e-08 ) ; ( R ) = ( 3.18e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30731229.692690186 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 30897550.812502872 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 30423133.450898774 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.158928 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0824255 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.06197e+07s, dt:126348s, Cycle: 396 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 6.84e-07 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.71e-05 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 4.71e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30779450.60628944 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 30945551.80080286 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 30471608.12308961 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.141047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.078531 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.07461e+07s, dt:116854s, Cycle: 397 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 6.54e-07 ) ; ( R ) = ( 5.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.80e-08 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.53e-06 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 9.53e-06 ) ; + Last LinSolve(iter,res) = ( 3, 7.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30823947.980949722 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 30989870.30823858 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 30516327.826228887 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.13066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727064 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.08629e+07s, dt:113918s, Cycle: 398 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 5.46e-07 ) ; ( R ) = ( 5.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.92e-05 ) ; ( Rwell ) = ( 5.52e-08 ) ; ( R ) = ( 4.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30867305.96913902 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 31033118.884777535 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 30559937.104967996 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.126173 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0591186 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.09768e+07s, dt:127088s, Cycle: 399 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 5.56e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 7.76e-07 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-04 ) ; ( Rwell ) = ( 1.88e-08 ) ; ( R ) = ( 2.45e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 30915602.02728062 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 31081247.74693252 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 30608507.586114235 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.139367 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0536016 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.11039e+07s, dt:150610s, Cycle: 400 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-06 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 1.81e-06 ) ; + Last LinSolve(iter,res) = ( 7, 9.04e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 30972760.559902918 Pa +wellControls1: Total rate: 56.328373541922936 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026258 sm3/s +wellControls2: BHP (at the specified reference elevation): 31138119.32740094 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 30665958.78412667 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.163366 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0745049 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.12545e+07s, dt:144414s, Cycle: 401 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 6.72e-10 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 9.71e-07 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 4.84e-08 ) ; ( R ) = ( 7.17e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31027343.031029046 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 31192457.99967053 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 30720812.08314479 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.156036 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618248 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.1399e+07s, dt:156607s, Cycle: 402 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 6.38e-08 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 2.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.58e-06 ) ; ( Rwell ) = ( 2.51e-09 ) ; ( R ) = ( 9.58e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31086307.566808783 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31251111.534945194 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 30780043.788147297 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.168421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.07134 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.15556e+07s, dt:154633s, Cycle: 403 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.70e-08 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-05 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 1.16e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31144356.961251847 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls2: BHP (at the specified reference elevation): 31308903.256142292 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 30838375.069120742 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.166475 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.108237 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.17102e+07s, dt:113354s, Cycle: 404 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 9.28e-07 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31187123.4001905 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31351487.16322151 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 30881339.916435614 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.122789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0760512 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.18236e+07s, dt:107177s, Cycle: 405 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 7.39e-07 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.04e-05 ) ; ( Rwell ) = ( 9.39e-09 ) ; ( R ) = ( 6.04e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31227664.676316757 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 31391793.07752773 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 30922060.259778444 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.116729 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.063487 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.19307e+07s, dt:114265s, Cycle: 406 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 9.85e-09 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 9.37e-07 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.24e-05 ) ; ( Rwell ) = ( 2.76e-08 ) ; ( R ) = ( 9.24e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.39e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31270711.195695285 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31434671.542515315 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 30965341.25391571 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.123991 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631425 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.2045e+07s, dt:122249s, Cycle: 407 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.48e-06 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.48e-06 ) ; ( Rwell ) = ( 6.18e-10 ) ; ( R ) = ( 6.48e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31316894.326637052 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 31480674.57885752 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 31011798.808133677 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.132056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0845743 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.21672e+07s, dt:107349s, Cycle: 408 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 9.89e-10 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.47e-03 ) ; ( Rwell ) = ( 8.80e-07 ) ; ( R ) = ( 7.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.62e-05 ) ; ( Rwell ) = ( 6.60e-09 ) ; ( R ) = ( 4.62e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31357413.382828474 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31521023.43692959 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 31052539.118199054 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.117739 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0815614 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.22746e+07s, dt:96701.1s, Cycle: 409 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 6.60e-09 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 1.91e-06 ) ; ( R ) = ( 6.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.77e-05 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 3.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31393828.588810753 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 31557269.31196054 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 31089141.26923919 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.107453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0738207 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.23713e+07s, dt:93305.9s, Cycle: 410 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 9.20e-09 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 3.91e-07 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31429049.69314245 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31592372.147389457 Pa +wellControls2: Total rate: 56.32837354192298 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026592 sm3/s +wellControls3: BHP (at the specified reference elevation): 31124564.256299984 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.105764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661068 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.24646e+07s, dt:96898.8s, Cycle: 411 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 1.85e-06 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 9.26e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.81e-06 ) ; ( Rwell ) = ( 8.89e-10 ) ; ( R ) = ( 3.81e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31465697.930921447 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 31628906.288238887 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 31161435.35024031 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.103884 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0521748 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.25615e+07s, dt:116712s, Cycle: 412 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.21e-05 ) ; ( Rwell ) = ( 6.57e-09 ) ; ( R ) = ( 4.21e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31509744.233399875 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31672812.56282357 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 31205738.302200384 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.125006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.045574 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.26782e+07s, dt:152094s, Cycle: 413 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 7.02e-09 ) ; ( R ) = ( 4.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 9.51e-07 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-05 ) ; ( Rwell ) = ( 4.02e-09 ) ; ( R ) = ( 3.60e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31567269.073924422 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31730161.410047688 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 31263621.816871148 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.163238 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0738262 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.28303e+07s, dt:146746s, Cycle: 414 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 2.53e-06 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-04 ) ; ( Rwell ) = ( 3.01e-08 ) ; ( R ) = ( 2.42e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.19e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31622852.1431755 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31785637.577531952 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 31319602.61260404 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.156991 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648852 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.2977e+07s, dt:154261s, Cycle: 415 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 5.73e-07 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 2.77e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.65e-07 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.74e-06 ) ; ( Rwell ) = ( 3.08e-09 ) ; ( R ) = ( 8.74e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31681153.993265316 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 31843676.406247135 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 31378263.44089848 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.163599 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064118 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.31313e+07s, dt:163415s, Cycle: 416 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.20e-05 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 9.20e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31743013.669370573 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 31905248.75136566 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 31440494.35570732 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.172342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677611 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.32947e+07s, dt:166975s, Cycle: 417 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 6.23e-07 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-04 ) ; ( Rwell ) = ( 6.23e-08 ) ; ( R ) = ( 2.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31805970.066173878 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 31967983.38435561 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 31503823.902257815 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.174547 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668265 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.34617e+07s, dt:172179s, Cycle: 418 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; ( R ) = ( 4.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.34e-06 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 8.30e-09 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31870735.125718 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 32032483.180058975 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270262836 sm3/s +wellControls3: BHP (at the specified reference elevation): 31568959.82297063 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.179015 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706273 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.36339e+07s, dt:171157s, Cycle: 419 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 8.40e-09 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 1.35e-06 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 6.70e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.12e-07 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.36e-06 ) ; ( Rwell ) = ( 6.44e-09 ) ; ( R ) = ( 4.36e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 31935171.329021353 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 32096702.97994291 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 31633790.53266217 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.180036 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678285 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.3805e+07s, dt:174771s, Cycle: 420 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 6.44e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32000889.261073772 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 32162183.66814443 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 31699886.572545644 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.188037 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.075007 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.39798e+07s, dt:166816s, Cycle: 421 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 5.60e-07 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-04 ) ; ( Rwell ) = ( 3.37e-08 ) ; ( R ) = ( 1.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32063659.27769131 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 32224684.608173925 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 31762998.871147387 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.182452 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662885 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.41466e+07s, dt:172929s, Cycle: 422 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 6.27e-07 ) ; ( R ) = ( 9.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 3.21e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.85e-06 ) ; ( Rwell ) = ( 2.58e-10 ) ; ( R ) = ( 2.85e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32128994.960168328 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 32289732.90598331 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 31828659.550544214 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.187478 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723236 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.43196e+07s, dt:169185s, Cycle: 423 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 6.89e-10 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 9.46e-07 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-05 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 5.03e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32193101.08332842 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 32353719.349452745 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 31893145.868683435 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.177913 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730521 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.44887e+07s, dt:164406s, Cycle: 424 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 9.95e-07 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 6.76e-08 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32255512.355646387 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 32416012.58753269 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 31955957.992783003 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.17271 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0859735 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.46531e+07s, dt:142698s, Cycle: 425 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 6.79e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 7.38e-07 ) ; ( R ) = ( 7.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.59e-05 ) ; ( Rwell ) = ( 1.80e-08 ) ; ( R ) = ( 6.59e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32309671.59503346 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 32470042.02064322 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 32010441.89154353 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.150352 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.081429 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.47958e+07s, dt:128690s, Cycle: 426 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 7.75e-07 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.42e-06 ) ; ( Rwell ) = ( 4.66e-10 ) ; ( R ) = ( 5.42e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32358417.16461451 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 32518682.520149194 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 32059488.306766324 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.137926 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737972 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.49245e+07s, dt:124199s, Cycle: 427 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 7.18e-10 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 6.54e-07 ) ; ( R ) = ( 9.01e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; ( R ) = ( 2.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32405392.319757476 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 32565573.446742896 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 32106758.46879051 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.134987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656797 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.50487e+07s, dt:129528s, Cycle: 428 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 4.39e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 7.55e-07 ) ; ( R ) = ( 9.35e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-05 ) ; ( Rwell ) = ( 5.47e-09 ) ; ( R ) = ( 2.28e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32454429.132576484 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 32614525.04994119 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 32156107.931654062 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.140863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0576172 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.51783e+07s, dt:146846s, Cycle: 429 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 7.97e-07 ) ; ( R ) = ( 3.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; ( R ) = ( 8.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32509999.501979414 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 32669965.73597748 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 32212036.892936435 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.156789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0513836 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.53251e+07s, dt:178493s, Cycle: 430 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.74e-02 ) ; ( Rwell ) = ( 6.86e-07 ) ; ( R ) = ( 7.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.44e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.48e-07 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 4.60e-09 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32577453.072344474 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 32737260.9705202 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 32279931.357940964 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.186355 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.052014 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.55036e+07s, dt:215387s, Cycle: 431 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.60e-09 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 1.77e-06 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 8.89e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 9.12e-07 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 9.00e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.45e-07 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.70e-07 ) ; ( Rwell ) = ( 8.37e-10 ) ; ( R ) = ( 7.70e-07 ) ; + Last LinSolve(iter,res) = ( 7, 2.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32658776.06709086 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 32818405.92618445 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 32361747.440936178 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.224728 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0592121 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.5719e+07s, dt:240051s, Cycle: 432 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 5.97e-10 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 1.78e-06 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 8.89e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 4.44e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.43e-06 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32749259.403034814 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 32908689.95924893 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls3: BHP (at the specified reference elevation): 32452774.20293797 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.246907 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0768251 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.5959e+07s, dt:225399s, Cycle: 433 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 8.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32834614.805180237 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 32993857.053545997 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls3: BHP (at the specified reference elevation): 32538631.02241551 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.230903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0738527 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.61844e+07s, dt:217422s, Cycle: 434 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.75e-06 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-04 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 2.17e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 32917012.331489995 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 33075947.71507691 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 32621482.368533604 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.221724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652316 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.64019e+07s, dt:227765s, Cycle: 435 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 1.80e-06 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.24e-05 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.24e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33003042.069583 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 33161717.658973597 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 32707984.050800722 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.232324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0586341 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.66296e+07s, dt:255413s, Cycle: 436 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.94e-06 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.26e-08 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.96e-06 ) ; ( Rwell ) = ( 5.08e-10 ) ; ( R ) = ( 1.96e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33099388.015808348 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 33257817.170255773 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 32804879.614035342 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260904 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681067 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.6885e+07s, dt:260103s, Cycle: 437 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 5.80e-10 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 6.77e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33197900.4840149 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 33356134.71991418 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 32903974.951208267 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.268636 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755052 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.71451e+07s, dt:158863s, Cycle: 438 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 9.97e-09 ) ; ( R ) = ( 3.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.87e-08 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.00e-06 ) ; ( Rwell ) = ( 8.57e-10 ) ; ( R ) = ( 9.00e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33258409.644550744 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 33416470.567504223 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 32964796.940600038 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.165519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0483685 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.7304e+07s, dt:200083s, Cycle: 439 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 7.76e-10 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.76e-05 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 4.76e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33334463.139726434 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 33492369.15541522 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 33041317.845760465 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.207695 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601532 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.75041e+07s, dt:220788s, Cycle: 440 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.38e-05 ) ; ( Rwell ) = ( 1.96e-08 ) ; ( R ) = ( 3.38e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33418527.61653162 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 33576317.35090382 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 33125915.96247958 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.227702 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613078 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.77249e+07s, dt:240715s, Cycle: 441 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 9.27e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.00e-05 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 6.00e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33509933.345624976 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 33667572.08787271 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 33217866.95627542 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.244483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652779 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.79656e+07s, dt:252051s, Cycle: 442 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-04 ) ; ( Rwell ) = ( 2.75e-08 ) ; ( R ) = ( 1.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33605310.03316257 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 33762838.68039544 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 33313823.923094295 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254862 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727265 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.82176e+07s, dt:245671s, Cycle: 443 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 1.54e-06 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.11e-07 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 3.11e-07 ) ; + Last LinSolve(iter,res) = ( 7, 8.26e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 33698011.17849388 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 33855403.91406805 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 33407096.155586682 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250583 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0714369 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.84633e+07s, dt:242355s, Cycle: 444 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 5.59e-10 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.51e-06 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 1.84e-08 ) ; ( R ) = ( 6.39e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33789647.7722823 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 33946979.14328152 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 33499320.45291593 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066456 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.87057e+07s, dt:250821s, Cycle: 445 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.90e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 8.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 7.57e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 7.53e-07 ) ; ( R ) = ( 7.81e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-04 ) ; ( Rwell ) = ( 8.07e-09 ) ; ( R ) = ( 1.28e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33884579.691390544 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 34041762.46100605 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 33594785.35261428 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.25812 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0811622 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.89565e+07s, dt:226719s, Cycle: 446 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 7.68e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.56e-03 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 9.56e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 33970283.054924 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 34127364.03712656 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 33681002.82937277 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.230019 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0860192 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.91832e+07s, dt:196708s, Cycle: 447 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 1.10e-06 ) ; ( R ) = ( 7.64e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 9.12e-09 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34044523.17393064 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 34201498.355845526 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 33755689.3550525 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.196344 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762535 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.93799e+07s, dt:185651s, Cycle: 448 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 5.66e-07 ) ; ( R ) = ( 6.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.86e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.73e-07 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.17e-05 ) ; ( Rwell ) = ( 8.73e-08 ) ; ( R ) = ( 7.17e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34114534.31011114 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 34271382.20033824 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 33826092.9225768 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.185268 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639478 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.95656e+07s, dt:197007s, Cycle: 449 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 8.73e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 6.42e-07 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 7.05e-08 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34188814.05570214 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 34345559.900703594 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 33900800.07584399 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195471 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055076 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.97626e+07s, dt:229648s, Cycle: 450 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 7.05e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.24e-06 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 4.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34275482.26692823 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 34432200.572647765 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 33987975.61694665 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22553 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0482616 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.99922e+07s, dt:289605s, Cycle: 451 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.24e-06 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.30e-08 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-06 ) ; ( Rwell ) = ( 3.00e-10 ) ; ( R ) = ( 3.21e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34384524.48304343 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 34541147.04923222 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 34097634.58594565 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281213 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070588 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.02818e+07s, dt:287992s, Cycle: 452 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 5.35e-10 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-04 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 1.38e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34492799.51152004 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 34649414.73078385 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 34206532.55226394 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0819549 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.05698e+07s, dt:258554s, Cycle: 453 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 6.02e-08 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 6.00e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.01e-07 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 6, 2.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.00e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.50e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 6.88e-09 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34589927.252687566 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 34746601.11813218 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 34304252.0298416 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737205 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.08284e+07s, dt:249707s, Cycle: 454 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 6.88e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 6.42e-08 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.86e-05 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 2.86e-05 ) ; + Last LinSolve(iter,res) = ( 2, 8.46e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34683831.3949422 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 34840565.863972455 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 34398764.62562345 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.239588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0724202 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.10781e+07s, dt:244081s, Cycle: 455 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-04 ) ; ( Rwell ) = ( 3.01e-08 ) ; ( R ) = ( 1.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34775682.944594964 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 34932448.60806282 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 34491192.37282192 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234413 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697893 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.13222e+07s, dt:244571s, Cycle: 456 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 5.84e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 5.96e-07 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.55e-05 ) ; ( Rwell ) = ( 1.93e-08 ) ; ( R ) = ( 8.55e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34867755.38778444 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 35024491.166520126 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 34583777.79652153 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.235021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0844561 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.15667e+07s, dt:214974s, Cycle: 457 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 1.15e-06 ) ; ( R ) = ( 7.08e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.21e-05 ) ; ( Rwell ) = ( 1.48e-08 ) ; ( R ) = ( 6.21e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 34948415.6173837 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 35105194.57831965 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 34664919.24470592 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.205742 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755268 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.17817e+07s, dt:204225s, Cycle: 458 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 6.13e-07 ) ; ( R ) = ( 8.73e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.53e-04 ) ; ( Rwell ) = ( 2.17e-08 ) ; ( R ) = ( 3.53e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35024968.74753171 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 35181834.822342075 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 34741919.20540248 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670519 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.19859e+07s, dt:210124s, Cycle: 459 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 1.57e-06 ) ; ( R ) = ( 7.23e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-05 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 2.72e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35104126.98465941 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 35260944.24495119 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 34821451.97448404 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.201278 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0702474 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.21961e+07s, dt:209630s, Cycle: 460 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 1.54e-06 ) ; ( R ) = ( 8.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 7.70e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 8.24e-07 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.25e-05 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 4.25e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35183214.10211643 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 35340088.84898461 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 34901003.9092208 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.201117 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640114 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.24057e+07s, dt:222310s, Cycle: 461 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 4.62e-09 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.69e-06 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.46e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 9.32e-07 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 1.88e-08 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35266902.38063198 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 35423857.920575805 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 34985221.074058846 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.210802 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566876 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.2628e+07s, dt:254588s, Cycle: 462 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.00e-06 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 8.67e-08 ) ; ( R ) = ( 8.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35362823.20414254 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 35519894.527231425 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 35081790.43732044 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.241412 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0530577 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.28826e+07s, dt:303570s, Cycle: 463 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 8.67e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 2.45e-06 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 6.47e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35477162.38588143 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 35634430.00472794 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 35196881.93926015 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.286937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0827238 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.31861e+07s, dt:270760s, Cycle: 464 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 9.98e-07 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.12e-05 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 9.12e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35579014.07787816 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 35736498.705390915 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 35299382.17409873 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.253794 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0802441 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.34569e+07s, dt:246692s, Cycle: 465 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 1.98e-06 ) ; ( R ) = ( 5.91e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.00e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-06 ) ; ( Rwell ) = ( 4.13e-09 ) ; ( R ) = ( 4.65e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35671866.144336104 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 35829405.8272429 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 35392710.42333654 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.230617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0707203 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.37036e+07s, dt:245011s, Cycle: 466 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 8.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35763749.19390772 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 35921387.31424436 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 35485113.305542774 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.228502 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.063921 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.39486e+07s, dt:260068s, Cycle: 467 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 5.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.65e-06 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.00e-05 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 9.00e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35861115.39139337 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 36018965.69221071 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 35583079.18237236 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.241731 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0571592 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.42087e+07s, dt:296304s, Cycle: 468 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.14e-06 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.78e-08 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.41e-06 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 9.41e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 35972052.16828138 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 36130199.7552622 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 35694706.98546135 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0522017 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.4505e+07s, dt:356781s, Cycle: 469 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-04 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 2.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 36105851.9676246 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 36264258.703706615 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls3: BHP (at the specified reference elevation): 35829210.120063394 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327716 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612326 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.48618e+07s, dt:389286s, Cycle: 470 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 2.69e-07 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.72e-08 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.40e-07 ) ; ( Rwell ) = ( 1.87e-10 ) ; ( R ) = ( 2.40e-07 ) ; + Last LinSolve(iter,res) = ( 8, 7.92e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 36251254.81461204 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 36410062.5368634 Pa +wellControls2: Total rate: 56.32837354192298 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls3: BHP (at the specified reference elevation): 35975418.62054394 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723649 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.52511e+07s, dt:380711s, Cycle: 471 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 4.78e-10 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.09e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 9.29e-08 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-05 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 2.06e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 36393105.07227283 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 36552451.63225245 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls3: BHP (at the specified reference elevation): 36118100.77957708 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0731889 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.56318e+07s, dt:369490s, Cycle: 472 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.59e-05 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.59e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 36531315.6408524 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 36691132.471082665 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 36257064.24421688 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343243 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716839 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.60013e+07s, dt:363658s, Cycle: 473 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 5.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 1.75e-07 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 8.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 9.82e-08 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.53e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 36667697.54203567 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 36827834.963620104 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 36394004.88785387 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.33436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688906 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.63649e+07s, dt:367541s, Cycle: 474 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.84e-07 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.57e-07 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.65e-05 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 7.65e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 36805745.04933192 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 36966275.22467361 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls3: BHP (at the specified reference elevation): 36532729.01540965 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.333468 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648295 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.67324e+07s, dt:386577s, Cycle: 475 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 5.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 1.72e-07 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-04 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 2.77e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 36951081.72377078 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 37112108.51352939 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 36678793.2358164 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.351828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658139 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.7119e+07s, dt:402629s, Cycle: 476 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.85e-07 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-04 ) ; ( Rwell ) = ( 3.37e-08 ) ; ( R ) = ( 1.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 37101883.33941678 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 37263440.29263429 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 36830288.0423336 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.361619 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689438 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.75217e+07s, dt:406720s, Cycle: 477 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.96e-07 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.28e-07 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-06 ) ; ( Rwell ) = ( 6.39e-09 ) ; ( R ) = ( 3.08e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.29e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 37253707.380838595 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 37415461.753585145 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 36982515.33023523 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.364604 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655905 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.79284e+07s, dt:424549s, Cycle: 478 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 6.39e-09 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 2.12e-07 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-04 ) ; ( Rwell ) = ( 4.91e-08 ) ; ( R ) = ( 1.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 37411529.8986726 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 37573581.05757745 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 37140804.60326524 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.383967 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721163 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.83529e+07s, dt:416161s, Cycle: 479 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 4.91e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.20e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 9.20e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.41e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.62e-03 ) ; ( Rwell ) = ( 2.68e-07 ) ; ( R ) = ( 7.62e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.46e-05 ) ; ( Rwell ) = ( 1.98e-08 ) ; ( R ) = ( 5.46e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 37566673.73208757 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 37729536.718148716 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 37296858.173431836 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.378584 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690877 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.87691e+07s, dt:419808s, Cycle: 480 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 5.46e-07 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.63e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.55e-03 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 8.55e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.82e-04 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 3.82e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 37722394.79917167 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 37886446.07793337 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 37453920.795274556 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.373496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636222 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.91889e+07s, dt:446957s, Cycle: 481 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 7.26e-07 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 3.49e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.38e-07 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.61e-05 ) ; ( Rwell ) = ( 2.56e-08 ) ; ( R ) = ( 6.61e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 37888186.17845454 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 38053882.39010949 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 37621468.14794214 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.386195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0731253 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.96359e+07s, dt:434038s, Cycle: 482 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.58e-06 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-04 ) ; ( Rwell ) = ( 2.69e-08 ) ; ( R ) = ( 2.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 38049483.333309695 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 38216681.62323236 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 37784663.70153467 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.374351 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753134 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.00699e+07s, dt:413132s, Cycle: 483 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; ( R ) = ( 5.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.51e-02 ) ; ( Rwell ) = ( 1.09e-06 ) ; ( R ) = ( 8.51e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 5.53e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 5.44e-07 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-05 ) ; ( Rwell ) = ( 6.15e-08 ) ; ( R ) = ( 5.72e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 38203124.68302162 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 38371319.40416876 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 37940188.7232432 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.355965 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737685 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.0483e+07s, dt:398818s, Cycle: 484 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 6.15e-08 ) ; ( R ) = ( 5.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-04 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 2.29e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 38351437.61973123 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 38520569.37918981 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 38090148.70982301 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343654 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681907 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.08818e+07s, dt:405811s, Cycle: 485 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; ( R ) = ( 5.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.84e-06 ) ; ( Rwell ) = ( 2.72e-10 ) ; ( R ) = ( 2.84e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 38502411.361081086 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 38672458.614519455 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 38242626.84693956 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.349637 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621534 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.12877e+07s, dt:438587s, Cycle: 486 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 4.78e-10 ) ; ( R ) = ( 5.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 5.50e-07 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.84e-05 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 2.84e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.75e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 38665767.494493954 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 38836701.31595842 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 38407158.72287676 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.377232 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.05631 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.17262e+07s, dt:500000s, Cycle: 487 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.98e-10 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 1.15e-06 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 5.75e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 9.26e-07 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-04 ) ; ( Rwell ) = ( 5.09e-08 ) ; ( R ) = ( 2.80e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 38851902.23450265 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 39023792.49584437 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 38594121.54496977 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.428128 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0617799 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.22262e+07s, dt:500000s, Cycle: 488 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 1.68e-06 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 8.63e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 8.04e-07 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.20e-04 ) ; ( Rwell ) = ( 5.66e-08 ) ; ( R ) = ( 2.20e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39037758.89630377 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 39210664.548933566 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 38780614.63546419 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.424409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692425 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.27262e+07s, dt:345762s, Cycle: 489 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 5.66e-08 ) ; ( R ) = ( 3.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.22e-07 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.91e-06 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 5.91e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39166280.73693672 Pa +wellControls1: Total rate: 56.328373541922936 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026283 sm3/s +wellControls2: BHP (at the specified reference elevation): 39339864.97722055 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 38909535.2977324 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.290321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0532034 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.3072e+07s, dt:411606s, Cycle: 490 +compflowStatistics, Reservoir: Pressure (min, average, max): 4.0589e+07, 4.24547e+07, 4.37795e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 2.79555e+07, 3.11457e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.70236e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 74795.6, 6.69488e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 5.91645e+07, 6.6046e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.96345e+07, 1.98362e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 3.953e+07, 4.62098e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 381538, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 5.8783e+07, 6.6046e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 5.91645e+07, 0 }, { 5.1921e+07, 6.59929e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 4.01373e+07, 4.14981e+07, 4.2362e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 2.75038e+07, 2.97282e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.3125e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 50868.2, 1.30742e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 3.99598e+07, 1.28933e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 9.15288e+06, 3.88321e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 3.08069e+07, 9.01006e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 102973, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 3.98568e+07, 1.28933e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 3.99598e+07, 0 }, { 2.94342e+07, 1.28632e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 3.78442e+07, 3.95078e+07, 4.18484e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 2.52109e+07, 2.92148e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.33182e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 1.22242e+07, 1.20958e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 9.29219e+09, 1.19299e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 9.28467e+08, 3.94396e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 8.36372e+09, 7.98592e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 5.86702e+06, 3.432e+08 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 9.28632e+09, 1.18956e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 9.29219e+09, 0 }, { 1.08538e+09, 1.18188e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 4.14495e+07, 4.44983e+07, 4.61001e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 2.88159e+07, 3.34661e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.10956e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 25659.3, 1.1093e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 2.05405e+07, 1.09573e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 6.20907e+06, 3.28796e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 1.43315e+07, 7.66934e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 2.05405e+07, 1.09573e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 2.05405e+07, 0 }, { 1.28865e+07, 1.0956e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 3.8077e+07, 4.46565e+07, 4.6874e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 2.54434e+07, 3.42399e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.40837e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 1949.89, 6.40818e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 1.50352e+06, 6.33053e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 1.08749e+06, 1.89922e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 416036, 4.43131e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 607224, 0 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 896298, 6.33053e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 1.50352e+06, 0 }, { 1.19316e+07, 6.32932e+10 } } kg +compflowStatistics: Max phase CFL number: 2.69398 +compflowStatistics: Max component CFL number: 5.51704 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.86e-08 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-06 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 1.69e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39319064.07552079 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 39493442.73025825 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 39062830.259178035 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341868 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668928 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.34836e+07s, dt:424157s, Cycle: 491 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 1.11e-06 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 5.53e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 5.99e-07 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-05 ) ; ( Rwell ) = ( 3.15e-08 ) ; ( R ) = ( 1.71e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39476574.690979384 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 39652002.57831442 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 39220898.03554483 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.352639 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691009 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.39078e+07s, dt:427821s, Cycle: 492 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.69e-08 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.30e-06 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 8.30e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.59e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39635337.788564794 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 39811793.40466466 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 39380290.72714503 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.356459 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0772155 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.43356e+07s, dt:400312s, Cycle: 493 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 5.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 3.62e-07 ) ; ( R ) = ( 2.96e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.12e-07 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-06 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 4.17e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39784053.61108188 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 39961325.9650537 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 39529563.46607975 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.334361 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0735477 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.47359e+07s, dt:387229s, Cycle: 494 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 2.62e-07 ) ; ( R ) = ( 1.80e-01 ) ; + Last LinSolve(iter,res) = ( 9, 4.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 6.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.01e-07 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.51e-05 ) ; ( Rwell ) = ( 1.48e-08 ) ; ( R ) = ( 9.51e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 39927926.7760402 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 40105988.941315055 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 39674030.36648245 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.321804 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666454 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.51231e+07s, dt:400008s, Cycle: 495 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 5.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.97e-07 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 5.28e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 40076609.9515448 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 40255522.07874718 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 39823406.54807389 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335404 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0610378 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.55231e+07s, dt:437337s, Cycle: 496 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 4.91e-07 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 8.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 40239936.98373206 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 40419819.557468526 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 39987653.50727036 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367572 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697451 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.59605e+07s, dt:438401s, Cycle: 497 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.58e-02 ) ; ( Rwell ) = ( 1.97e-06 ) ; ( R ) = ( 9.58e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 9.74e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 9.75e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 9.75e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 5.04e-07 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 40403745.28130031 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 40584612.64645983 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 40152407.54070052 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.364174 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0764417 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.63989e+07s, dt:413060s, Cycle: 498 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 5.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.36e-05 ) ; ( Rwell ) = ( 2.78e-07 ) ; ( R ) = ( 7.36e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 40557554.31753809 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 40739370.04770441 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 40307108.211817965 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0732158 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.68119e+07s, dt:400786s, Cycle: 499 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 2.78e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 1.18e-07 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 40706446.287290044 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 40889192.65990962 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 40456894.673830576 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332155 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666129 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.72127e+07s, dt:414145s, Cycle: 500 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.18e-07 ) ; ( R ) = ( 5.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 3.91e-07 ) ; ( R ) = ( 6.72e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.55e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 1.86e-07 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.20e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.38e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 1.51e-07 ) ; ( R ) = ( 6.64e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-05 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 2.10e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 40860258.70463891 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 41044042.18148539 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 40611587.19463551 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.339129 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694601 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.76269e+07s, dt:416286s, Cycle: 501 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 5.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 3.96e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-05 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 1.83e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.49e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41014733.19298061 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 41199652.748340555 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 40766996.055183105 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667247 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.80431e+07s, dt:429689s, Cycle: 502 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 5.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 3.33e-07 ) ; ( R ) = ( 6.74e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.67e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.24e-07 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 8, 2.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41174332.92453822 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 41360570.91324598 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 40927608.48444648 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064619 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.84728e+07s, dt:452899s, Cycle: 503 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 4.58e-07 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.23e-07 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.35e-06 ) ; ( Rwell ) = ( 2.39e-10 ) ; ( R ) = ( 4.35e-06 ) ; + Last LinSolve(iter,res) = ( 9, 1.05e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41342619.09053745 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 41530261.23070727 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 41097000.38122043 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.366887 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691891 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.89257e+07s, dt:456424s, Cycle: 504 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.96e-10 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 5.24e-07 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 1.84e-07 ) ; ( R ) = ( 7.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41512463.81534878 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 41701496.114866085 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 41267915.4514264 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.372674 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644649 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.93822e+07s, dt:481824s, Cycle: 505 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.84e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 5.42e-07 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 4.63e-08 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.25e-06 ) ; ( Rwell ) = ( 5.12e-09 ) ; ( R ) = ( 8.25e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41691821.834334806 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 41882314.45424218 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 41448374.91612011 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.392038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0857561 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.9864e+07s, dt:418956s, Cycle: 506 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 5.12e-09 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.90e-07 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-04 ) ; ( Rwell ) = ( 1.42e-07 ) ; ( R ) = ( 2.55e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41847659.908456214 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 42039474.39596344 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 41605195.42898382 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335732 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.080409 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.02829e+07s, dt:381169s, Cycle: 507 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 1.42e-07 ) ; ( R ) = ( 5.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 4.59e-07 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.67e-05 ) ; ( Rwell ) = ( 5.39e-08 ) ; ( R ) = ( 6.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.04e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 41989443.171067655 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 42182441.78576214 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 41747899.4474167 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303956 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0719183 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.06641e+07s, dt:374331s, Cycle: 508 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 5.94e-07 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.49e-07 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-06 ) ; ( Rwell ) = ( 2.71e-10 ) ; ( R ) = ( 2.69e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 42128855.06559945 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 42322993.15214014 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 41888206.85324105 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299806 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643222 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.10384e+07s, dt:395729s, Cycle: 509 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 5.16e-10 ) ; ( R ) = ( 5.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 6.60e-07 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-04 ) ; ( Rwell ) = ( 9.26e-08 ) ; ( R ) = ( 2.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 42276382.83385286 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls2: BHP (at the specified reference elevation): 42471808.36150347 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 42036709.07273138 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.318128 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613421 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.14342e+07s, dt:431292s, Cycle: 510 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 9.26e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.77e-07 ) ; ( R ) = ( 4.24e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 8.56e-08 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 8.40e-09 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 42436983.775123656 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 42633704.895925865 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls3: BHP (at the specified reference elevation): 42198352.52785012 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070132 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.18655e+07s, dt:430750s, Cycle: 511 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 8.40e-09 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 3.37e-07 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-04 ) ; ( Rwell ) = ( 8.56e-08 ) ; ( R ) = ( 2.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 42597121.2405698 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 42795094.58148438 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026258 sm3/s +wellControls3: BHP (at the specified reference elevation): 42359493.77569173 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.339234 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687956 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.22962e+07s, dt:435749s, Cycle: 512 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 8.53e-08 ) ; ( R ) = ( 5.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.73e-02 ) ; ( Rwell ) = ( 3.06e-07 ) ; ( R ) = ( 8.73e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.24e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.86e-05 ) ; ( Rwell ) = ( 1.96e-08 ) ; ( R ) = ( 6.86e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 42758811.079457715 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 42958078.241149895 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 42522235.36804471 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.339387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633556 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.2732e+07s, dt:465186s, Cycle: 513 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 5.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 2.82e-07 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-04 ) ; ( Rwell ) = ( 2.90e-07 ) ; ( R ) = ( 2.73e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 42931187.24214124 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 43131798.924418636 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 42695745.0021291 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.363102 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631538 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.31971e+07s, dt:497632s, Cycle: 514 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.90e-07 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 3.01e-07 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.96e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.93e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 3.80e-07 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.86e-05 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 2.86e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 43115231.76725212 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 43317309.057960965 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 42881031.417347424 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.386616 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0749932 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.36948e+07s, dt:475042s, Cycle: 515 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.28e-07 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.14e-07 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-05 ) ; ( Rwell ) = ( 6.75e-09 ) ; ( R ) = ( 1.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 43291341.75491845 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 43494827.49527088 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 43058350.86011222 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369163 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.072476 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.41698e+07s, dt:464098s, Cycle: 516 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 6.75e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.78e-07 ) ; ( R ) = ( 3.85e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 2.29e-07 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-05 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 1.00e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 43463398.81951462 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 43668253.531395905 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 43231593.6660804 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357018 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671051 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.46339e+07s, dt:477256s, Cycle: 517 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 6.13e-07 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.27e-07 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.34e-06 ) ; ( Rwell ) = ( 4.95e-09 ) ; ( R ) = ( 3.34e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 43639446.246135004 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 43845656.98316101 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 43408898.55760149 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.359914 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623031 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.51112e+07s, dt:500000s, Cycle: 518 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 4.95e-09 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 8.23e-07 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 1.66e-07 ) ; ( R ) = ( 9.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 43823622.74582416 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 44031215.31504876 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 43594418.17807119 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.376059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065412 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.56112e+07s, dt:500000s, Cycle: 519 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.66e-07 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 8.18e-07 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-04 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 3.14e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44007058.10513938 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 44216061.82332073 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 43779194.285057075 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.377026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0693738 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.61112e+07s, dt:500000s, Cycle: 520 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 6.86e-07 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 3.65e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.29e-07 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-04 ) ; ( Rwell ) = ( 4.71e-08 ) ; ( R ) = ( 2.04e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44190977.24689065 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 44401442.929717585 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 43964459.46766445 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.378983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0789244 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.66112e+07s, dt:460832s, Cycle: 521 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; ( R ) = ( 5.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.31e-07 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 5.48e-08 ) ; ( R ) = ( 7.22e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44361097.52333675 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 44572962.83076832 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 44135868.90007514 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.348076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0781783 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.7072e+07s, dt:427532s, Cycle: 522 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 5.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.05e-07 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-04 ) ; ( Rwell ) = ( 1.71e-07 ) ; ( R ) = ( 2.09e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44518658.49123038 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 44731731.97889955 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 44294631.50533664 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.317505 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737218 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.74995e+07s, dt:412897s, Cycle: 523 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.71e-07 ) ; ( R ) = ( 5.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.02e-07 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.80e-08 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.68e-05 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 7.68e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44670872.72778586 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 44885057.040497966 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 44447981.80517608 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675874 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.79124e+07s, dt:422607s, Cycle: 524 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.91e-07 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44826547.92561771 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 45041873.28552692 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 44604849.20116398 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.315309 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0595337 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.8335e+07s, dt:469396s, Cycle: 525 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 6.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 9.87e-08 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 7.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 5.07e-08 ) ; ( R ) = ( 7.22e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 44999741.72909275 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 45216248.87454649 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 44779339.82745797 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.349755 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0563893 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.88044e+07s, dt:35561.7s, Cycle: 526 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 3.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.26e-05 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.26e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45012855.80829598 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 45229509.397905126 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 44792619.25598603 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0274184 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00422211 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.884e+07s, dt:71123.3s, Cycle: 527 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-04 ) ; ( Rwell ) = ( 5.48e-07 ) ; ( R ) = ( 4.69e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45039213.06050487 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 45256066.19992114 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 44819160.56451817 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0530848 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00826208 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.89111e+07s, dt:142247s, Cycle: 528 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.48e-07 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.24e-07 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.45e-05 ) ; ( Rwell ) = ( 1.72e-08 ) ; ( R ) = ( 5.45e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45091961.377582334 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 45309151.49764642 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 44872249.935357414 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.105702 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0157672 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.90534e+07s, dt:284493s, Cycle: 529 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 2.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.03e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.58e-05 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 9.58e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.79e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45197317.9497464 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 45415278.986026056 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 44978430.95335336 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.209774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0316559 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.93379e+07s, dt:448149s, Cycle: 530 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 3.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 2.24e-07 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 10, 2.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.79e-07 ) ; ( Rwell ) = ( 1.89e-10 ) ; ( R ) = ( 9.79e-07 ) ; + Last LinSolve(iter,res) = ( 6, 1.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45362972.47428221 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 45582069.17797927 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 45145389.300551854 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.325187 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055302 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.9786e+07s, dt:500000s, Cycle: 531 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.30e-10 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 8.06e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 5.10e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45547450.2415931 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 45767847.639812 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 45331322.75473918 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35873 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650373 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.0286e+07s, dt:500000s, Cycle: 532 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 7.49e-07 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-05 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 1.03e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45731937.79001164 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 45953604.152427 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 45517312.45500101 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.359045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677634 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.0786e+07s, dt:500000s, Cycle: 533 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 7.59e-07 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 4.55e-08 ) ; ( R ) = ( 4.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 45916352.96705016 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 46139164.20436239 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 45703194.5412004 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.359418 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681945 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.1286e+07s, dt:500000s, Cycle: 534 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; ( R ) = ( 5.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 6.30e-07 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 46100302.13289666 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 46324269.600076854 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 45888624.60290605 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358647 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649189 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.1786e+07s, dt:500000s, Cycle: 535 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 6.92e-07 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.51e-08 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 8, 3.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.33e-05 ) ; ( Rwell ) = ( 4.68e-09 ) ; ( R ) = ( 4.33e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.29e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 46284541.520859234 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 46509754.89886481 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 46074395.096865505 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0615301 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.2286e+07s, dt:500000s, Cycle: 536 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 6.71e-07 ) ; ( R ) = ( 3.51e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.11e-08 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-05 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 1.14e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.53e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 46469271.009960994 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 46695691.55959594 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 46260673.82597546 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.3594 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568515 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.2786e+07s, dt:500000s, Cycle: 537 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 4.23e-07 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.28e-05 ) ; ( Rwell ) = ( 2.52e-09 ) ; ( R ) = ( 9.28e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 46653965.44904668 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 46881519.57184101 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 46446938.25826925 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.360952 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0550383 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.3286e+07s, dt:500000s, Cycle: 538 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 8.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 46838486.55344247 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 47067167.296722606 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 46633066.47114472 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358404 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575979 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.3786e+07s, dt:500000s, Cycle: 539 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 3.65e-07 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 8.29e-08 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 47022762.365744755 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 47252604.75390309 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 46818972.07420395 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.352619 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0587556 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.4286e+07s, dt:500000s, Cycle: 540 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.74e-07 ) ; ( R ) = ( 4.81e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.86e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.87e-07 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.86e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 10, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.74e-06 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 6.74e-06 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 47206818.3143011 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 47437819.806244165 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 47004667.54099437 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.349648 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594593 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.4786e+07s, dt:500000s, Cycle: 541 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 4.38e-07 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 2.20e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 3.30e-07 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.20e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 1.46e-07 ) ; ( R ) = ( 6.98e-03 ) ; + Last LinSolve(iter,res) = ( 10, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.14e-05 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 6.14e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 47390643.002322584 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 47622725.03114754 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 47190129.52711733 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.347699 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598846 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.5286e+07s, dt:500000s, Cycle: 542 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.98e-07 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.36e-08 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-06 ) ; ( Rwell ) = ( 6.90e-10 ) ; ( R ) = ( 4.20e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 47574458.39967617 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 47807588.37118468 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 47375585.62841368 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345855 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0587124 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.5786e+07s, dt:500000s, Cycle: 543 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 8.10e-10 ) ; ( R ) = ( 4.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.74e-02 ) ; ( Rwell ) = ( 2.20e-07 ) ; ( R ) = ( 7.74e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.24e-07 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-04 ) ; ( Rwell ) = ( 3.15e-08 ) ; ( R ) = ( 1.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 47758446.702175036 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 47992527.581738636 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 47561184.14641078 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.344621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.062407 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.6286e+07s, dt:500000s, Cycle: 544 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.61e-02 ) ; ( Rwell ) = ( 4.68e-07 ) ; ( R ) = ( 9.61e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 2.50e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.50e-04 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 3.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 47942376.44906683 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 48177358.982099526 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 47746740.14303109 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646428 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.6786e+07s, dt:500000s, Cycle: 545 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 5.03e-07 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 10, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.85e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 1.75e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.98e-07 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.91e-04 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 1.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 48126095.33168621 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 48362002.85344829 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 47932137.498103194 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065381 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.7286e+07s, dt:500000s, Cycle: 546 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 4.04e-07 ) ; ( R ) = ( 3.36e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 7.32e-08 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-05 ) ; ( Rwell ) = ( 6.67e-09 ) ; ( R ) = ( 4.65e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 48309706.22889482 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 48546514.35891037 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 48117475.104719006 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345014 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.072299 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.7786e+07s, dt:489287s, Cycle: 547 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 6.67e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.45e-07 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.26e-08 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.96e-05 ) ; ( Rwell ) = ( 6.54e-10 ) ; ( R ) = ( 8.96e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 48489079.716566026 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 48726707.197933935 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 48298540.95382642 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.336799 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0740999 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.82753e+07s, dt:470900s, Cycle: 548 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 8.40e-10 ) ; ( R ) = ( 5.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 1.62e-07 ) ; ( R ) = ( 7.77e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 7.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.03e-07 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-05 ) ; ( Rwell ) = ( 3.10e-08 ) ; ( R ) = ( 3.37e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 48661474.45217746 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 48899919.5455638 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 48472578.72701631 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.321593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069104 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.87462e+07s, dt:474952s, Cycle: 549 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 4.13e-07 ) ; ( R ) = ( 7.84e-03 ) ; + Last LinSolve(iter,res) = ( 10, 4.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.56e-08 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.35e-06 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 6.35e-06 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 48835321.85122782 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 49074572.563346975 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 48648130.83356644 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623992 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.92212e+07s, dt:500000s, Cycle: 550 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 4.18e-07 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.10e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 3.14e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.71e-08 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-05 ) ; ( Rwell ) = ( 9.90e-09 ) ; ( R ) = ( 1.16e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 49018502.64253914 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 49258590.211097926 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 48833121.81771495 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.33387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0516239 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.97212e+07s, dt:500000s, Cycle: 551 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 9.90e-09 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 6.53e-07 ) ; ( R ) = ( 3.16e-02 ) ; + Last LinSolve(iter,res) = ( 10, 2.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 1.17e-07 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-06 ) ; ( Rwell ) = ( 8.80e-10 ) ; ( R ) = ( 2.96e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 49201987.784871385 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 49442862.56186763 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 49018381.40139454 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.33367 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518858 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.02212e+07s, dt:500000s, Cycle: 552 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 4.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 6.45e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.29e-08 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-05 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 1.41e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 49385864.96662694 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 49627434.480745904 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 49204015.613173485 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.333609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0539665 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.07212e+07s, dt:500000s, Cycle: 553 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 8.24e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.33e-08 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.88e-06 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 9.88e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 49569415.50122881 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 49811661.531353876 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 49389371.28356398 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.331936 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059073 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.12212e+07s, dt:500000s, Cycle: 554 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 8.32e-07 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 9.88e-08 ) ; ( R ) = ( 4.00e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 49752822.9149973 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 49995687.11941442 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 49574600.32800496 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.330895 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0608059 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.17212e+07s, dt:500000s, Cycle: 555 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 9.88e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 8.58e-07 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.76e-05 ) ; ( Rwell ) = ( 2.72e-08 ) ; ( R ) = ( 8.76e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 49936183.61894497 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 50179713.9498505 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 49759792.03557887 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.329921 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0620743 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.22212e+07s, dt:500000s, Cycle: 556 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 8.25e-07 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 6.74e-08 ) ; ( R ) = ( 5.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 50119314.773957476 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 50363474.27286735 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 49944771.50016044 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678607 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.27212e+07s, dt:500000s, Cycle: 557 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 6.74e-08 ) ; ( R ) = ( 5.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 8.64e-07 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.72e-08 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.93e-06 ) ; ( Rwell ) = ( 3.03e-10 ) ; ( R ) = ( 2.93e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 50302704.31202209 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 50547377.49567611 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 50129989.45865028 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686602 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.32212e+07s, dt:500000s, Cycle: 558 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 4.79e-10 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 6.74e-07 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.63e-05 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 9.63e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 50486251.955359444 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 50731416.57258361 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 50315368.18847848 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.328275 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716898 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.37212e+07s, dt:492081s, Cycle: 559 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 5.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 6.94e-07 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 4.52e-08 ) ; ( R ) = ( 5.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 50666717.24975288 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 50912348.371832505 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 50497635.6322398 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324326 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723375 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.42132e+07s, dt:394768s, Cycle: 560 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 7.21e-07 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 2.35e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 50811619.36591529 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 51057694.313598156 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 50644014.37274087 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260866 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0559475 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.4608e+07s, dt:455764s, Cycle: 561 +compflowStatistics, Reservoir: Pressure (min, average, max): 5.26089e+07, 5.44914e+07, 5.58276e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 3.99598e+07, 4.31781e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.73814e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 191642, 6.71898e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 1.6394e+08, 6.68349e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 4.49606e+07, 2.01084e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 1.18979e+08, 4.67265e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.38745e+06, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.62552e+08, 6.68349e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 1.6394e+08, 0 }, { 1.06591e+08, 6.67257e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 5.21529e+07, 5.35266e+07, 5.43982e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 3.95038e+07, 4.17489e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.31951e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 92946.4, 1.31021e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 7.91269e+07, 1.30302e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 1.84898e+07, 3.93715e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 6.06371e+07, 9.0931e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 611891, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 7.8515e+07, 1.30302e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 7.91269e+07, 0 }, { 4.92449e+07, 1.29798e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 4.98416e+07, 5.15207e+07, 5.38802e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 3.71928e+07, 4.12309e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.33893e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 1.66107e+07, 1.17282e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 1.38573e+10, 1.16686e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.29852e+09, 4.00046e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 1.25588e+10, 7.66819e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 9.94063e+06, 1.51449e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 1.38473e+10, 1.15172e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 1.38573e+10, 0 }, { 1.38456e+09, 1.15265e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 5.34771e+07, 5.65521e+07, 5.81674e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 4.08279e+07, 4.55177e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.11549e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 112242, 1.11436e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 9.69655e+07, 1.10974e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 2.44663e+07, 3.33261e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 7.24993e+07, 7.76478e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 943828, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 9.60217e+07, 1.10974e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 9.69655e+07, 0 }, { 5.24673e+07, 1.1092e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 5.0095e+07, 5.67114e+07, 5.89475e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 3.7446e+07, 4.62977e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.4426e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 100283, 6.43257e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 8.43458e+07, 6.40661e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 9.6428e+06, 1.92501e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 7.4703e+07, 4.4816e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 307514, 0 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 8.40382e+07, 6.40661e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 8.43458e+07, 0 }, { 3.28412e+07, 6.40327e+10 } } kg +compflowStatistics: Max phase CFL number: 2.0683 +compflowStatistics: Max component CFL number: 4.10467 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 5.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.95e-07 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 8, 3.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.73e-04 ) ; ( Rwell ) = ( 3.47e-08 ) ; ( R ) = ( 3.73e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 50978648.45436127 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 51225132.18772825 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 50812749.616579756 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299227 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0579009 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.50638e+07s, dt:500000s, Cycle: 562 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 7.33e-08 ) ; ( R ) = ( 8.06e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 51161862.16408792 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 51408745.01183519 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 50997808.6585072 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690051 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.55638e+07s, dt:500000s, Cycle: 563 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 7.30e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.34e-02 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 8.34e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 6.07e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 3.17e-07 ) ; ( R ) = ( 9.06e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.47e-06 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 7.47e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 51344917.638710104 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 51592185.55743578 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 51182711.015612274 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737964 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.60638e+07s, dt:482553s, Cycle: 564 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 5.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 5.58e-07 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.51e-07 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.15e-06 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 2.15e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 51521060.928809136 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 51768660.5204796 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 51360612.62485068 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0710921 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.65463e+07s, dt:477586s, Cycle: 565 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.35e-07 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-05 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 1.20e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 51695021.99444459 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 51942904.68062294 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 51536305.7899445 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654134 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.70239e+07s, dt:499401s, Cycle: 566 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; ( R ) = ( 5.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 7.77e-07 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-04 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 3.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 51876969.081511274 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 52125089.003904335 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 51720048.75464168 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.317146 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059042 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.75233e+07s, dt:500000s, Cycle: 567 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 9.90e-07 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.21e-07 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.52e-06 ) ; ( Rwell ) = ( 4.79e-10 ) ; ( R ) = ( 3.52e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 52058979.09489201 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 52307325.16550613 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 51903863.70622583 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.315525 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0523573 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.80233e+07s, dt:500000s, Cycle: 568 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 6.44e-10 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 4.61e-07 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 2.31e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.46e-08 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 6.34e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 52241431.48119863 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 52489935.17303858 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 52088093.06889739 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.31427 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0560691 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.85233e+07s, dt:500000s, Cycle: 569 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 7.10e-07 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.23e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.17e-06 ) ; ( Rwell ) = ( 4.03e-09 ) ; ( R ) = ( 5.17e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 52424107.501851976 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 52672759.28911544 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 52272535.429858744 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.312403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593467 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.90233e+07s, dt:500000s, Cycle: 570 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.13e-08 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-05 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 1.56e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.27e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 52606798.84701645 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 52855558.95543003 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 52456963.65986723 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.310252 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06068 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.95233e+07s, dt:500000s, Cycle: 571 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.98e-07 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 6.83e-08 ) ; ( R ) = ( 6.53e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 52789063.28473837 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 53037859.80485123 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 52640919.7572105 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308865 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0597494 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00023e+08s, dt:500000s, Cycle: 572 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 4.78e-07 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 9.87e-08 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.98e-05 ) ; ( Rwell ) = ( 8.21e-09 ) ; ( R ) = ( 1.98e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 52971076.789534606 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 53219882.05063644 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 52824587.51874688 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613525 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00523e+08s, dt:500000s, Cycle: 573 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 8.21e-09 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-04 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 3.19e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 53152959.789565444 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 53401721.47867977 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 53008089.42804541 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307651 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0597645 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01023e+08s, dt:500000s, Cycle: 574 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 9.45e-07 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.77e-06 ) ; ( Rwell ) = ( 5.07e-10 ) ; ( R ) = ( 2.77e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 53335052.33580715 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 53583767.142846674 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 53191810.15469244 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307471 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0603081 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01523e+08s, dt:500000s, Cycle: 575 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 5.07e-10 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 4.89e-07 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 7.01e-08 ) ; ( R ) = ( 7.06e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 53517069.91390118 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 53765749.46613767 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 53375422.340094395 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653339 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02023e+08s, dt:500000s, Cycle: 576 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 6.99e-08 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.49e-08 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-06 ) ; ( Rwell ) = ( 9.60e-10 ) ; ( R ) = ( 1.81e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 53698803.18120819 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 53947382.678121716 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 53558759.157514915 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303838 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681204 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02523e+08s, dt:500000s, Cycle: 577 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 9.60e-10 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.29e-07 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 6.13e-08 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 53880521.33297805 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 54128974.256801665 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 53742054.76122622 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303463 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683282 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03023e+08s, dt:500000s, Cycle: 578 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; ( R ) = ( 5.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 8.05e-07 ) ; ( R ) = ( 7.79e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 5.15e-08 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 54062385.84869939 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 54310712.96339403 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 53925471.64411028 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303885 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064701 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03523e+08s, dt:500000s, Cycle: 579 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 3.44e-07 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 6.17e-08 ) ; ( R ) = ( 6.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.66e-05 ) ; ( Rwell ) = ( 7.46e-09 ) ; ( R ) = ( 7.66e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 54244629.53304954 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 54492798.311424196 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 54109194.38486773 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.304674 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568675 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.04023e+08s, dt:500000s, Cycle: 580 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 7.46e-09 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.88e-07 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 4.71e-08 ) ; ( R ) = ( 9.04e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 54427287.69165677 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 54675307.44475994 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 54293313.72071281 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30348 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0587597 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.04523e+08s, dt:500000s, Cycle: 581 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.88e-07 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 4.83e-08 ) ; ( R ) = ( 6.61e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 54609691.90841391 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 54857507.93129125 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 54477146.97535881 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.300839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0616917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.05023e+08s, dt:500000s, Cycle: 582 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 6.45e-07 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-04 ) ; ( Rwell ) = ( 4.03e-08 ) ; ( R ) = ( 2.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 54791582.1078026 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 55039125.55440799 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 54660361.0145073 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299591 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653687 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.05523e+08s, dt:500000s, Cycle: 583 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; ( R ) = ( 5.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 5.38e-07 ) ; ( R ) = ( 4.17e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 1.78e-08 ) ; ( R ) = ( 6.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 54973428.629115865 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 55220736.644909665 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 54843504.90926648 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.298813 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669652 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.06023e+08s, dt:500000s, Cycle: 584 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; ( R ) = ( 5.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 5.95e-07 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.77e-08 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.38e-06 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 3.38e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 55155211.45843424 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 55402286.87524419 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 55026532.263900414 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.298 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646118 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.06523e+08s, dt:500000s, Cycle: 585 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 6.38e-07 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 7.76e-08 ) ; ( R ) = ( 9.04e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 55337167.185407914 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 55584010.86971975 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 55209718.078690015 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.297201 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585169 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.07023e+08s, dt:500000s, Cycle: 586 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 7.76e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-04 ) ; ( Rwell ) = ( 9.45e-08 ) ; ( R ) = ( 1.57e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.33e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 55519281.23215802 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 55765853.533436045 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 55393022.115601815 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.296543 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0504817 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.07523e+08s, dt:500000s, Cycle: 587 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 9.45e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 1.21e-06 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 6.54e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 6.40e-07 ) ; ( R ) = ( 7.22e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.97e-05 ) ; ( Rwell ) = ( 2.15e-08 ) ; ( R ) = ( 7.97e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 55701317.13610154 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 55947562.42034948 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 55576164.21290239 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.293972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0450987 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08023e+08s, dt:500000s, Cycle: 588 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.24e-06 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 9.38e-08 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.87e-06 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 8.87e-06 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 55883428.56370598 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 56129305.77542416 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 55759346.0167885 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.293338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0485246 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08523e+08s, dt:500000s, Cycle: 589 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.28e-06 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 8.98e-08 ) ; ( R ) = ( 5.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 56065596.889457405 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 56311130.2755738 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 55942541.05367039 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.29253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0539885 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.09023e+08s, dt:500000s, Cycle: 590 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 8.96e-08 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 2.29e-07 ) ; ( R ) = ( 9.81e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-04 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 1.64e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.29e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 56248077.4791878 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 56493305.40006254 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 56126011.595189646 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.291886 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565272 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.09523e+08s, dt:500000s, Cycle: 591 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 2.24e-07 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.02e-05 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 6.02e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 56430866.36895102 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 56675776.3869769 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 56309718.8325786 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.29176 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0562239 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.10023e+08s, dt:352696s, Cycle: 592 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.75e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 56559857.84855528 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 56804504.7527112 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 56439324.325948596 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.205681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0384491 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.10376e+08s, dt:500000s, Cycle: 593 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 1.75e-07 ) ; ( R ) = ( 9.78e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 9.41e-09 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 56742384.85500851 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 56986605.68188348 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 56622654.33511277 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.290187 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0506038 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.10876e+08s, dt:500000s, Cycle: 594 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 9.41e-09 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.56e-07 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 7.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 7.25e-08 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.57e-05 ) ; ( Rwell ) = ( 2.83e-08 ) ; ( R ) = ( 5.57e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 56924498.79402304 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 57168285.77425783 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 56805514.8235079 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.287602 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0453932 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.11376e+08s, dt:500000s, Cycle: 595 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; ( R ) = ( 3.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 5.51e-07 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.22e-05 ) ; ( Rwell ) = ( 2.86e-08 ) ; ( R ) = ( 7.22e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 57106489.17638861 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 57349856.34977851 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 56988211.686338 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.286998 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0456848 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.11876e+08s, dt:500000s, Cycle: 596 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 5.35e-07 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 57288171.62647993 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 57531127.06801434 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 57170569.37402368 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.286625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0451591 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.12376e+08s, dt:500000s, Cycle: 597 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 5.41e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 57469970.72775069 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 57712503.306422 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 57352993.16605104 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.287068 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.04323 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.12876e+08s, dt:500000s, Cycle: 598 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.19e-07 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.03e-08 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.69e-06 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 8.69e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 57652071.019239366 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 57894199.18159519 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 57535735.21999058 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.28753 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0451059 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13376e+08s, dt:500000s, Cycle: 599 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 5.72e-07 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 5.32e-08 ) ; ( R ) = ( 4.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 57834100.364890225 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 58075838.80527802 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 57718395.15296035 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.286527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0437703 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13876e+08s, dt:500000s, Cycle: 600 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 5.30e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 6.34e-07 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-04 ) ; ( Rwell ) = ( 2.95e-08 ) ; ( R ) = ( 3.00e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 58016082.863655016 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 58257427.88957845 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 57900985.6933546 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.284651 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0444529 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14376e+08s, dt:500000s, Cycle: 601 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 4.79e-07 ) ; ( R ) = ( 7.65e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.67e-08 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.75e-06 ) ; ( Rwell ) = ( 7.30e-10 ) ; ( R ) = ( 3.75e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 58198068.546401806 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 58438993.82521157 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 58083563.262057275 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.28245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0486844 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14876e+08s, dt:500000s, Cycle: 602 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 6.09e-10 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 2.65e-07 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 6.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 58379874.175599225 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 58620406.44908284 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 58265970.34376534 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.280464 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051253 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15376e+08s, dt:500000s, Cycle: 603 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.39e-07 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.06e-08 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-06 ) ; ( Rwell ) = ( 2.03e-09 ) ; ( R ) = ( 3.62e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 58561852.86093394 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 58802002.14512334 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 58448549.591268666 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593294 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15876e+08s, dt:500000s, Cycle: 604 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.81e-07 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.24e-08 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-05 ) ; ( Rwell ) = ( 5.02e-09 ) ; ( R ) = ( 1.55e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 58743850.26927373 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 58983578.81273186 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 58631119.293777235 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676584 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.16376e+08s, dt:500000s, Cycle: 605 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 1.99e-08 ) ; ( R ) = ( 4.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 58925945.98881291 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 59165278.58451769 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 58813783.47022672 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278255 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0710428 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.16876e+08s, dt:495083s, Cycle: 606 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-04 ) ; ( Rwell ) = ( 3.27e-08 ) ; ( R ) = ( 2.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 59106162.94006988 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 59345098.98541526 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 58994565.45857731 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274882 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689955 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.17371e+08s, dt:499865s, Cycle: 607 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; ( R ) = ( 5.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 2.27e-07 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 6.92e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 59288217.80687745 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 59526741.0589353 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 59177133.47465175 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.277383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0790699 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.17871e+08s, dt:460120s, Cycle: 608 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 5.47e-07 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 4.12e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 59455889.33101477 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 59694068.779155046 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 59345249.3959065 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255758 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0756692 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.18331e+08s, dt:436550s, Cycle: 609 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 5.42e-07 ) ; ( R ) = ( 9.91e-03 ) ; + Last LinSolve(iter,res) = ( 8, 3.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.22e-05 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 5.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 59614925.19805299 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 59852802.16313183 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 59504717.71167826 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.242674 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687668 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18768e+08s, dt:441738s, Cycle: 610 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 6.79e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.88e-05 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 6.88e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 59775739.71268044 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 60013314.0409666 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 59665976.347081214 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.244961 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0614212 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.19209e+08s, dt:481040s, Cycle: 611 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 7.02e-07 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-04 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 1.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 59950923.18808466 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 60188146.00349222 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 59841631.7973077 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.26467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.053156 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.1969e+08s, dt:500000s, Cycle: 612 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 6.47e-07 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.49e-05 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 7.49e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 60132610.002970986 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 60369498.00937869 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 60023821.07040783 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.272871 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0406653 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2019e+08s, dt:500000s, Cycle: 613 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 3.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 6.38e-07 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.19e-08 ) ; ( R ) = ( 7.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 60314201.775005735 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 60550793.590246804 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 60205944.84661316 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.272215 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0408858 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2069e+08s, dt:500000s, Cycle: 614 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 5.74e-07 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-04 ) ; ( Rwell ) = ( 7.07e-08 ) ; ( R ) = ( 1.41e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 60495658.44608719 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 60731946.46004442 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 60387935.80817084 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.271241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0427206 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2119e+08s, dt:500000s, Cycle: 615 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 7.07e-08 ) ; ( R ) = ( 3.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.63e-07 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.72e-05 ) ; ( Rwell ) = ( 6.00e-08 ) ; ( R ) = ( 9.72e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 60677291.71065427 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 60913300.01632203 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 60570124.730658665 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.270356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0451582 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2169e+08s, dt:500000s, Cycle: 616 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.35e-07 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.40e-05 ) ; ( Rwell ) = ( 2.03e-08 ) ; ( R ) = ( 7.40e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 60859096.9771605 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 61094819.851586364 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 60752502.13058524 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.269507 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0422921 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2219e+08s, dt:500000s, Cycle: 617 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; ( R ) = ( 3.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 2.43e-07 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 61041050.63387366 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 61276541.43397917 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 60935054.700038925 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.269116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0418514 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2269e+08s, dt:500000s, Cycle: 618 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 9.97e-08 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.26e-06 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 6.26e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 61223081.10097647 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 61458310.04023486 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 61117675.876052774 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.268592 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0448788 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2319e+08s, dt:500000s, Cycle: 619 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; ( R ) = ( 3.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.97e-07 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 3.21e-08 ) ; ( R ) = ( 2.10e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 61405317.020449765 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 61640312.28264858 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 61300507.209215224 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.268079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0474367 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2369e+08s, dt:500000s, Cycle: 620 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; ( R ) = ( 3.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-04 ) ; ( Rwell ) = ( 2.91e-08 ) ; ( R ) = ( 2.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 61587349.59220857 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 61822085.51190555 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 61483113.40217633 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266333 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0486052 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2419e+08s, dt:500000s, Cycle: 621 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.83e-03 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 8.83e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 7.97e-09 ) ; ( R ) = ( 9.23e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 61769227.908663705 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 62003748.47791152 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 61665593.38549657 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.265762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051117 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2469e+08s, dt:500000s, Cycle: 622 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 9.59e-07 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-04 ) ; ( Rwell ) = ( 5.67e-08 ) ; ( R ) = ( 1.49e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 61950722.10729152 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 62185056.75510788 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 61847700.491295114 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.265152 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0533486 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2519e+08s, dt:500000s, Cycle: 623 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 5.67e-08 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.62e-03 ) ; ( Rwell ) = ( 2.47e-07 ) ; ( R ) = ( 8.62e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 9.06e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 62132243.83269527 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 62366384.78549509 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 62029866.70923121 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.265112 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.053218 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2569e+08s, dt:453604s, Cycle: 624 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 4.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 1.80e-07 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-05 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 3.31e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 62297055.54937715 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 62531033.28823988 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 62195267.21498203 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.240556 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0464889 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.26144e+08s, dt:500000s, Cycle: 625 +compflowStatistics, Reservoir: Pressure (min, average, max): 6.43651e+07, 6.62629e+07, 6.76094e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 5.16972e+07, 5.49412e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.77313e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 438360, 6.7293e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 3.95217e+08, 6.74688e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 9.357e+07, 2.03742e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 3.01647e+08, 4.70946e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.56947e+06, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 3.93648e+08, 6.74688e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 3.95217e+08, 0 }, { 2.02327e+08, 6.72608e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 6.39053e+07, 6.52902e+07, 6.61686e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 5.12375e+07, 5.35006e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.32636e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 159743, 1.31039e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 1.43528e+08, 1.31363e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 2.92901e+07, 3.98954e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 1.14238e+08, 9.14679e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 914275, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 1.42613e+08, 1.31363e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 1.43528e+08, 0 }, { 7.26099e+07, 1.30617e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 6.15671e+07, 6.32682e+07, 6.56463e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 4.88997e+07, 5.29783e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.34588e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.03201e+07, 1.14268e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 1.79934e+10, 1.14618e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.63116e+09, 4.05364e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 1.63622e+10, 7.4082e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 1.26036e+07, 2.71498e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 1.79808e+10, 1.11903e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 1.79934e+10, 0 }, { 1.65662e+09, 1.12914e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 6.52401e+07, 6.83399e+07, 6.99674e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 5.25722e+07, 5.7299e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12128e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 370589, 1.11757e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 3.36315e+08, 1.1216e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 7.28037e+07, 3.37611e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 2.63512e+08, 7.83991e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 1.56896e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 3.34746e+08, 1.1216e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 3.36315e+08, 0 }, { 1.4195e+08, 1.12014e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 6.18355e+07, 6.85e+07, 7.07537e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 4.91679e+07, 5.80852e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.47607e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 239051, 6.45217e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 2.12878e+08, 6.47561e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 2.02835e+07, 1.94995e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 1.92595e+08, 4.52566e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 250772, 0 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 2.12628e+08, 6.47561e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 2.12878e+08, 0 }, { 5.49816e+07, 6.47e+10 } } kg +compflowStatistics: Max phase CFL number: 1.72296 +compflowStatistics: Max component CFL number: 3.01345 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 5.08e-07 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 6.86e-08 ) ; ( R ) = ( 6.25e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 62478769.68073736 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 62712589.18374019 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 62377627.87867508 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.26454 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.047965 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.26644e+08s, dt:500000s, Cycle: 626 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 6.86e-08 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.61e-05 ) ; ( Rwell ) = ( 2.76e-08 ) ; ( R ) = ( 9.61e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 62660268.06335418 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 62893935.62556118 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 62559767.43140646 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.263003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0464511 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27144e+08s, dt:500000s, Cycle: 627 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; ( R ) = ( 3.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.63e-07 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.19e-05 ) ; ( Rwell ) = ( 3.36e-08 ) ; ( R ) = ( 6.19e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 62841686.26360695 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 63075191.79647743 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 62741826.21108159 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.261378 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0471563 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27644e+08s, dt:500000s, Cycle: 628 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 3.16e-07 ) ; ( R ) = ( 9.81e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-04 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 2.16e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 63023343.6151804 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 63256744.35725796 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 62924153.175259836 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.261107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0516826 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28144e+08s, dt:500000s, Cycle: 629 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 1.58e-07 ) ; ( R ) = ( 8.97e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 63204936.41552061 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 63438249.51557876 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 63106421.45847087 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260631 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055102 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28644e+08s, dt:500000s, Cycle: 630 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.58e-07 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.40e-02 ) ; ( Rwell ) = ( 3.25e-07 ) ; ( R ) = ( 7.40e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.42e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.36e-07 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.48e-05 ) ; ( Rwell ) = ( 7.16e-09 ) ; ( R ) = ( 4.48e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 63386391.77087556 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 63619610.53923799 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 63288575.66491856 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.258556 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566322 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29144e+08s, dt:500000s, Cycle: 631 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 7.16e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 3.22e-07 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.09e-05 ) ; ( Rwell ) = ( 2.79e-08 ) ; ( R ) = ( 9.09e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 63567809.79004053 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 63800923.53236312 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 63470671.56435802 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.257864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0509869 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29644e+08s, dt:500000s, Cycle: 632 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-05 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 7.21e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 63749157.512279935 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 63982120.12402488 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 63652672.7002994 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.257013 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0465182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.30144e+08s, dt:500000s, Cycle: 633 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.12e-06 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 1.13e-07 ) ; ( R ) = ( 3.71e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 63930629.39088623 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 64163502.24933304 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 63834830.018633984 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.25653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.045349 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.30644e+08s, dt:500000s, Cycle: 634 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 1.13e-07 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.40e-06 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.23e-08 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.20e-04 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.20e-04 ) ; + Last LinSolve(iter,res) = ( 6, 1.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 64112277.48471776 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 64345035.30282048 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 64017161.73107925 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255645 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0492787 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31144e+08s, dt:500000s, Cycle: 635 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.22e-03 ) ; ( Rwell ) = ( 1.78e-06 ) ; ( R ) = ( 9.22e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.99e-08 ) ; ( R ) = ( 5.94e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 64294074.2484452 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 64526741.016300045 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 64199677.58309096 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.25521 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0500412 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31644e+08s, dt:500000s, Cycle: 636 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.76e-06 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.12e-05 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 6.12e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 64475703.100787066 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 64708309.87783703 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 64382019.964358985 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254339 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0482528 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32144e+08s, dt:500000s, Cycle: 637 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 1.40e-06 ) ; ( R ) = ( 9.95e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.21e-08 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 64657026.02786486 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 64889571.36308596 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 64564067.69986929 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.253262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0449722 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32644e+08s, dt:500000s, Cycle: 638 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 3.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 2.53e-08 ) ; ( R ) = ( 4.64e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 64838107.248549774 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 65070588.43282399 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 64745879.671580575 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.252253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0424867 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33144e+08s, dt:500000s, Cycle: 639 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; ( R ) = ( 3.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.82e-07 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.11e-08 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.84e-06 ) ; ( Rwell ) = ( 7.24e-09 ) ; ( R ) = ( 8.84e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 65019529.54305707 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 65252001.71437163 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 64928030.50902708 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.252107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0414279 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33644e+08s, dt:500000s, Cycle: 640 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 7.24e-09 ) ; ( R ) = ( 3.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 9.48e-07 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.22e-05 ) ; ( Rwell ) = ( 8.27e-08 ) ; ( R ) = ( 6.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 65200752.2662642 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 65433182.71693161 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 65109971.99552683 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.251155 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0390263 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34144e+08s, dt:500000s, Cycle: 641 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 8.27e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 9.97e-07 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 65382195.92733517 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 65614596.11294759 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 65292129.76834485 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250799 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0358902 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34644e+08s, dt:500000s, Cycle: 642 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.75e-09 ) ; ( R ) = ( 3.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.02e-05 ) ; ( Rwell ) = ( 7.69e-08 ) ; ( R ) = ( 6.02e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 65563720.51354372 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 65796061.251580834 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 65474383.18808824 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.040971 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35144e+08s, dt:500000s, Cycle: 643 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 7.69e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 6.96e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 9.37e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 65745012.42128058 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 65977327.9650303 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 65656395.62558015 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0462563 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35644e+08s, dt:500000s, Cycle: 644 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.23e-03 ) ; ( Rwell ) = ( 4.46e-07 ) ; ( R ) = ( 6.23e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; ( R ) = ( 2.45e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 65926286.49162724 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 66158553.350811325 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 65838388.30039234 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.248625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0496576 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36144e+08s, dt:500000s, Cycle: 645 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 6.50e-09 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.28e-05 ) ; ( Rwell ) = ( 1.75e-08 ) ; ( R ) = ( 3.28e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 66107799.610788256 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 66340091.04594159 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 66020625.230119295 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.248369 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0508158 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36644e+08s, dt:500000s, Cycle: 646 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 8.07e-07 ) ; ( R ) = ( 6.08e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-05 ) ; ( Rwell ) = ( 9.97e-09 ) ; ( R ) = ( 3.21e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 66289582.04044159 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 66521899.68814367 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 66203155.17024228 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.248106 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.049651 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.37144e+08s, dt:500000s, Cycle: 647 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 9.85e-09 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.49e-05 ) ; ( Rwell ) = ( 8.30e-08 ) ; ( R ) = ( 9.49e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 66471554.53353049 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 66703915.68712637 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 66385871.578875445 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.247738 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0465464 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.37644e+08s, dt:500000s, Cycle: 648 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 8.30e-08 ) ; ( R ) = ( 3.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 9.78e-07 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.03e-05 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 4.03e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 66653405.51514404 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 66885756.877357006 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 66568458.80845425 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.246892 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0421963 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38144e+08s, dt:500000s, Cycle: 649 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 3.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 9.50e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-04 ) ; ( Rwell ) = ( 6.97e-08 ) ; ( R ) = ( 3.25e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 66835309.710965924 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 67067636.19178053 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 66751085.114470124 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.246324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0376745 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38644e+08s, dt:500000s, Cycle: 650 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 6.97e-08 ) ; ( R ) = ( 3.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.76e-03 ) ; ( Rwell ) = ( 1.58e-07 ) ; ( R ) = ( 7.76e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.68e-05 ) ; ( Rwell ) = ( 5.32e-08 ) ; ( R ) = ( 4.68e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 67016995.51113717 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 67249313.86335444 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 66933496.00350546 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.245427 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0385819 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39144e+08s, dt:500000s, Cycle: 651 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-05 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 3.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 67198557.32534842 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 67430870.3799866 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 67115794.70379137 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.244635 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0443578 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39644e+08s, dt:500000s, Cycle: 652 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; ( R ) = ( 3.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 1.69e-06 ) ; ( R ) = ( 6.95e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 6.57e-08 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 67380146.40780854 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 67612484.23689386 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 67298116.99955323 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.244087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0482345 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.40144e+08s, dt:500000s, Cycle: 653 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 6.57e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 1.71e-06 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.82e-05 ) ; ( Rwell ) = ( 1.45e-08 ) ; ( R ) = ( 5.82e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 67561908.85519364 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 67794312.54564641 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 67480626.33657557 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243744 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0496671 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.40644e+08s, dt:500000s, Cycle: 654 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 1.81e-06 ) ; ( R ) = ( 7.04e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-06 ) ; ( Rwell ) = ( 5.28e-09 ) ; ( R ) = ( 1.99e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 67743819.07430513 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 67976272.44248626 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 67663272.27065308 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0485162 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41144e+08s, dt:500000s, Cycle: 655 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 5.28e-09 ) ; ( R ) = ( 4.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 1.83e-06 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-05 ) ; ( Rwell ) = ( 1.38e-07 ) ; ( R ) = ( 4.66e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 67925631.91914642 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 68158117.95015348 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 67845810.16573353 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.242572 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0452227 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41644e+08s, dt:268000s, Cycle: 656 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.38e-07 ) ; ( R ) = ( 2.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.30e-07 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 7, 3.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-05 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 1.48e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 68023119.75664006 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 68255634.85261406 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 67943678.80463736 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.129879 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0229347 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41912e+08s, dt:485719s, Cycle: 657 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.19e-07 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.07e-04 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 5.07e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 68199605.07431388 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 68432163.84294963 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 68120867.22318707 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234577 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.036968 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.42398e+08s, dt:500000s, Cycle: 658 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.27e-07 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-04 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 1.71e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 68381460.88632454 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 68614063.00955157 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 68303442.03824887 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.241136 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0407002 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.42898e+08s, dt:500000s, Cycle: 659 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.43e-03 ) ; ( Rwell ) = ( 2.03e-07 ) ; ( R ) = ( 8.43e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.85e-04 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 3.85e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 68563416.5560494 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 68796071.6168393 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 68486162.07309419 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.240881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0476954 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43398e+08s, dt:500000s, Cycle: 660 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-04 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 2.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 68745101.62754905 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 68977826.40583465 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 68668596.4925625 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.240307 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0532396 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43898e+08s, dt:500000s, Cycle: 661 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 4.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 4.52e-07 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-04 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 4.73e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 68926610.43476327 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 69159413.83218354 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 68850854.8295143 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.239802 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.057018 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.44398e+08s, dt:500000s, Cycle: 662 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.83e-03 ) ; ( Rwell ) = ( 1.59e-07 ) ; ( R ) = ( 7.83e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-04 ) ; ( Rwell ) = ( 4.25e-08 ) ; ( R ) = ( 1.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 69108249.61976087 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls2: BHP (at the specified reference elevation): 69341107.83570576 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 69033242.7028452 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.239616 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0587841 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.44898e+08s, dt:500000s, Cycle: 663 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 5.27e-07 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.25e-05 ) ; ( Rwell ) = ( 6.31e-08 ) ; ( R ) = ( 4.25e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 69289874.56939736 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 69522803.4781063 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 69215620.14091326 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.238923 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0582171 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45398e+08s, dt:500000s, Cycle: 664 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 6.31e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.88e-07 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 3.65e-09 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 69471317.75402126 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 69704263.70227256 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 69397796.8389654 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.237785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0552351 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45898e+08s, dt:500000s, Cycle: 665 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 5.76e-07 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-05 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 3.57e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 69652552.3652561 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 69885522.8223925 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 69579768.74928206 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.236989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0500574 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.46398e+08s, dt:500000s, Cycle: 666 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 5.97e-07 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.14e-05 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 7.14e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 69833613.04964265 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 70066594.3025204 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 69761491.4504035 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.235814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0421512 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.46898e+08s, dt:500000s, Cycle: 667 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 3.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 4.09e-07 ) ; ( R ) = ( 9.06e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.86e-05 ) ; ( Rwell ) = ( 7.24e-08 ) ; ( R ) = ( 4.86e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 70014787.02285512 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 70247741.30049132 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 69943277.10998313 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234934 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0332519 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47398e+08s, dt:500000s, Cycle: 668 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 7.24e-08 ) ; ( R ) = ( 2.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.79e-05 ) ; ( Rwell ) = ( 8.84e-08 ) ; ( R ) = ( 6.79e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 70195989.47493446 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 70428944.84194592 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 70125109.4278724 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234443 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0339375 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47898e+08s, dt:500000s, Cycle: 669 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 8.84e-08 ) ; ( R ) = ( 2.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.67e-03 ) ; ( Rwell ) = ( 9.16e-08 ) ; ( R ) = ( 8.67e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.28e-04 ) ; ( Rwell ) = ( 1.06e-08 ) ; ( R ) = ( 3.28e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 70377451.7989477 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 70610396.20314053 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 70307190.35177608 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234193 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0342835 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48398e+08s, dt:500000s, Cycle: 670 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 2.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.52e-03 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 8.52e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 7.28e-08 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 70558992.09522364 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 70791923.5017565 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 70489348.209188 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0341337 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48898e+08s, dt:500000s, Cycle: 671 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 7.28e-08 ) ; ( R ) = ( 2.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.65e-03 ) ; ( Rwell ) = ( 3.88e-08 ) ; ( R ) = ( 8.65e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 5.49e-08 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 70740580.05916224 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 70973505.42342123 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 70671557.51866409 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233779 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0335336 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49398e+08s, dt:500000s, Cycle: 672 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 5.49e-08 ) ; ( R ) = ( 2.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 3.16e-08 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.98e-05 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 5.98e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 70922078.62306923 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 71155021.46733207 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 70853676.1736682 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233454 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0341033 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49898e+08s, dt:500000s, Cycle: 673 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 2.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 4.24e-08 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 8.78e-09 ) ; ( R ) = ( 9.29e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 71103445.69070779 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 71336407.65344526 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 71035658.02578957 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.232983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0323356 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50398e+08s, dt:500000s, Cycle: 674 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 8.87e-09 ) ; ( R ) = ( 2.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 5.19e-08 ) ; ( R ) = ( 8.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 71284723.45651396 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 71517699.36757407 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 71217547.81369781 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.232396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0291979 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50898e+08s, dt:500000s, Cycle: 675 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 6.13e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.37e-04 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 5.37e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 71466116.33152443 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 71699149.97582954 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 71399571.73905057 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.231737 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0283251 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.51398e+08s, dt:500000s, Cycle: 676 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 6.36e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 1.06e-08 ) ; ( R ) = ( 6.86e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 71647561.31800674 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 71880633.17587657 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 71581634.2189941 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.230785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0280603 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.51898e+08s, dt:500000s, Cycle: 677 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 2.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 1.54e-07 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.90e-05 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 7.90e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 71829038.39813392 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 72062127.41079614 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 71763738.92197023 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0283458 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52398e+08s, dt:500000s, Cycle: 678 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 2.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-04 ) ; ( Rwell ) = ( 6.82e-08 ) ; ( R ) = ( 3.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 72010626.82828178 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 72243733.03470176 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 71946012.398584 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22947 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0334726 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52898e+08s, dt:500000s, Cycle: 679 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 6.82e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.23e-07 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-05 ) ; ( Rwell ) = ( 4.02e-08 ) ; ( R ) = ( 2.67e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 72192181.33709161 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 72425319.9419448 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 72128238.93948154 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.228894 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0366951 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.53398e+08s, dt:500000s, Cycle: 680 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; ( R ) = ( 3.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 9.43e-08 ) ; ( R ) = ( 6.62e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.02e-05 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.02e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 72373688.31337303 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 72606837.97247258 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 72310401.97891705 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.228284 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0389671 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.53898e+08s, dt:500000s, Cycle: 681 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 3.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 9.30e-08 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.51e-05 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.51e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 72555241.49966608 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 72788397.62250952 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 72492599.41644737 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22781 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.040216 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54398e+08s, dt:500000s, Cycle: 682 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 9.30e-08 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.62e-04 ) ; ( Rwell ) = ( 2.86e-08 ) ; ( R ) = ( 2.62e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 72737010.48284024 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 72970172.05220515 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 72675027.27719882 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.227529 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0403933 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54898e+08s, dt:500000s, Cycle: 683 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; ( R ) = ( 3.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 9.24e-08 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 72918621.82185236 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 73151801.8999683 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 72857284.78019433 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.226838 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0395152 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55398e+08s, dt:500000s, Cycle: 684 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 3.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 7.35e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.94e-05 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 3.94e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 73100389.0866781 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 73333589.75978203 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 73039710.86836924 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.226496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0376923 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55898e+08s, dt:500000s, Cycle: 685 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 2.26e-07 ) ; ( R ) = ( 8.33e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.82e-04 ) ; ( Rwell ) = ( 2.57e-08 ) ; ( R ) = ( 3.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 73282145.0306834 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 73515389.96542889 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 73222121.50184464 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.225983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0351316 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56398e+08s, dt:500000s, Cycle: 686 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; ( R ) = ( 3.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 1.90e-07 ) ; ( R ) = ( 6.60e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 73463691.70563722 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 73696980.53446119 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 73404318.3858727 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.225214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0321041 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56898e+08s, dt:500000s, Cycle: 687 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 1.77e-07 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 73645197.10040407 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 73878522.62099978 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 73586474.62461393 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.224635 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0288742 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57398e+08s, dt:282281s, Cycle: 688 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; ( R ) = ( 1.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.79e-07 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.09e-06 ) ; ( Rwell ) = ( 5.26e-09 ) ; ( R ) = ( 4.09e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 73747638.94826588 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 73980997.47094513 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 73689284.29179366 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.126625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0163742 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.5768e+08s, dt:500000s, Cycle: 689 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.59999e+07, 7.79121e+07, 7.9268e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.3396e+07, 6.66638e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80776e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 805381, 6.72722e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 7.55396e+08, 6.79642e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.6611e+08, 2.06365e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 5.89286e+08, 4.73277e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 3.94608e+06, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 7.5145e+08, 6.79642e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 7.55396e+08, 0 }, { 3.27931e+08, 6.7626e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.55367e+07, 7.69319e+07, 7.78163e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.29328e+07, 6.52122e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33314e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 264592, 1.30668e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 2.475e+08, 1.32005e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 4.8316e+07, 4.04131e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 1.99184e+08, 9.15914e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 1.02126e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 2.46479e+08, 1.32005e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 2.475e+08, 0 }, { 1.02245e+08, 1.3095e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.31678e+07, 7.48935e+07, 7.72898e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.05642e+07, 6.46858e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35275e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.36205e+07, 1.11655e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.1853e+10, 1.12868e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.95034e+09, 4.10431e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 1.99027e+10, 7.18252e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 1.47121e+07, 3.92875e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.18383e+10, 1.0894e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.1853e+10, 0 }, { 1.90668e+09, 1.10901e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.68814e+07, 8.00047e+07, 8.16435e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.42775e+07, 6.90393e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12702e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 695083, 1.12007e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 6.55482e+08, 1.13249e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.28168e+08, 3.41882e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 5.27314e+08, 7.90604e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 3.083e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 6.52399e+08, 1.13249e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 6.55482e+08, 0 }, { 2.49814e+08, 1.12991e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.34481e+07, 8.01656e+07, 8.24355e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.08445e+07, 6.98312e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.5092e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 361181, 6.47308e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 3.35506e+08, 6.54438e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 2.97822e+07, 1.97438e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 3.05724e+08, 4.57e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 486896, 4.78481e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 3.35019e+08, 6.5439e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 3.35506e+08, 0 }, { 7.86924e+07, 6.53633e+10 } } kg +compflowStatistics: Max phase CFL number: 1.37485 +compflowStatistics: Max component CFL number: 2.59216 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 5.40e-09 ) ; ( R ) = ( 2.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 6.85e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-05 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 2.83e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 73929018.84604527 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 74162422.4001087 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 73871304.98770094 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.223667 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0297311 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5818e+08s, dt:500000s, Cycle: 690 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 2.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.18e-05 ) ; ( Rwell ) = ( 1.72e-08 ) ; ( R ) = ( 7.18e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 74110524.32945709 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 74343953.93447018 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 74053411.0274425 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.223283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0294182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5868e+08s, dt:500000s, Cycle: 691 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.98e-07 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 1.30e-08 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 74291990.81874774 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 74525434.5655354 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 74235280.48327066 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.222718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.029489 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5918e+08s, dt:500000s, Cycle: 692 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.69e-03 ) ; ( Rwell ) = ( 2.55e-07 ) ; ( R ) = ( 9.69e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 74473372.1988858 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 74706810.24815673 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 74417060.92454617 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.222119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0315188 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5968e+08s, dt:320000s, Cycle: 693 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 1.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.52e-06 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-05 ) ; ( Rwell ) = ( 2.99e-08 ) ; ( R ) = ( 1.46e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 74589483.77686697 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 74822928.03872411 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 74533426.15246576 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.141972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0208941 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6e+08s, dt:10000s, Cycle: 694 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 2.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.37e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.37e-05 ) ; + Last LinSolve(iter,res) = ( 3, 2.47e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0597402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00437265 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.6001e+08s, dt:20000s, Cycle: 695 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.47e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0071881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00877349 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.6003e+08s, dt:40000s, Cycle: 696 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.59e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00339072 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.01711 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.6007e+08s, dt:80000s, Cycle: 697 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.82e-04 ) ; + Last LinSolve(iter,res) = ( 3, 4.30e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00169211 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0324635 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6015e+08s, dt:124512s, Cycle: 698 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 2, 8.81e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00168819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0459025 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.60275e+08s, dt:161598s, Cycle: 699 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.25e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00211827 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0508748 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.60436e+08s, dt:197588s, Cycle: 700 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.06e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00252533 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0505455 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.60634e+08s, dt:242523s, Cycle: 701 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.33e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.33e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00297694 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0558588 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.60876e+08s, dt:280269s, Cycle: 702 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00326339 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.056697 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.61156e+08s, dt:320930s, Cycle: 703 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.57e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.58e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.49e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0035691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701735 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.61477e+08s, dt:320400s, Cycle: 704 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.33e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.38e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00353898 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658541 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.61798e+08s, dt:333571s, Cycle: 705 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.36e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.03e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00363067 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.62131e+08s, dt:378446s, Cycle: 706 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00400819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0489133 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6251e+08s, dt:473546s, Cycle: 707 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00467051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604717 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.62983e+08s, dt:520807s, Cycle: 708 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.44e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.87e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00488532 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607819 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.63504e+08s, dt:570929s, Cycle: 709 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.97e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00509105 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636827 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.64075e+08s, dt:607478s, Cycle: 710 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.01e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00514378 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0556907 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.64683e+08s, dt:703327s, Cycle: 711 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.69e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.69e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.97e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00564002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657308 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.65386e+08s, dt:733136s, Cycle: 712 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00527164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599219 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.66119e+08s, dt:810974s, Cycle: 713 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.70e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00550214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070001 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.6693e+08s, dt:810967s, Cycle: 714 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.35e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00547615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737686 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.67741e+08s, dt:782868s, Cycle: 715 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.47e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00541078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0680216 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.68524e+08s, dt:797902s, Cycle: 716 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.74e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00536996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602382 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.69322e+08s, dt:879686s, Cycle: 717 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.76e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00602964 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0530522 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.70201e+08s, dt:1.049e+06s, Cycle: 718 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.54e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00740578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557399 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.7125e+08s, dt:1.21386e+06s, Cycle: 719 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.04e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.91e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00758877 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544213 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.72464e+08s, dt:1.42533e+06s, Cycle: 720 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00849356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687656 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.7389e+08s, dt:1.44229e+06s, Cycle: 721 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00858781 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727385 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.75332e+08s, dt:1.40563e+06s, Cycle: 722 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.60e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.60e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.07e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00841086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0704205 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.76738e+08s, dt:1.40002e+06s, Cycle: 723 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.46e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.46e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.21e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00853464 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0807129 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.78138e+08s, dt:1.2704e+06s, Cycle: 724 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0075492 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.071317 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.79408e+08s, dt:1.25467e+06s, Cycle: 725 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-06 ) ; + Last LinSolve(iter,res) = ( 5, 9.92e-04 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00687178 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06323 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.80663e+08s, dt:1.34114e+06s, Cycle: 726 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.36e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.36e-07 ) ; + Last LinSolve(iter,res) = ( 6, 6.44e-04 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00659514 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657581 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.82004e+08s, dt:1.3976e+06s, Cycle: 727 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00663383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0799996 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.83401e+08s, dt:1.27607e+06s, Cycle: 728 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.14e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00595394 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0840388 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.84677e+08s, dt:1.12558e+06s, Cycle: 729 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00515561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0792625 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.85803e+08s, dt:1.03434e+06s, Cycle: 730 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.93e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.33e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00477247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0725523 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.86837e+08s, dt:1.00979e+06s, Cycle: 731 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00478941 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642457 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.87847e+08s, dt:1.06834e+06s, Cycle: 732 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.46e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.46e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.30e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.005205 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0543586 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.88916e+08s, dt:300491s, Cycle: 733 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.43e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00140989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0150582 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.89216e+08s, dt:600982s, Cycle: 734 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.67359e+07, 7.86499e+07, 8.00118e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.42369e+07, 6.75128e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80995e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 470485, 6.76291e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 4.42092e+08, 6.83696e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.93882e+08, 2.06554e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 2.4821e+08, 4.77143e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 5.78852e+06, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 4.36303e+08, 6.83696e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 4.42092e+08, 0 }, { 4.03949e+08, 6.79525e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.62718e+07, 7.76677e+07, 7.85587e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.37728e+07, 6.60596e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33357e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 169406, 1.31663e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 1.58747e+08, 1.33114e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 6.15633e+07, 4.0454e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 9.71839e+07, 9.26597e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 672313, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 1.58075e+08, 1.33114e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 1.58747e+08, 0 }, { 1.26211e+08, 1.3181e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.39078e+07, 7.56261e+07, 7.80315e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.14087e+07, 6.55324e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35319e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.44342e+07, 1.10884e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.26561e+10, 1.1217e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 2.07489e+09, 4.10841e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.05812e+10, 7.10863e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 1.49633e+07, 4.01511e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.26412e+10, 1.08155e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.26561e+10, 0 }, { 2.04804e+09, 1.10057e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.7619e+07, 8.07459e+07, 8.23891e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.512e+07, 6.98901e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12738e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 272909, 1.12465e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 2.5777e+08, 1.1378e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.39282e+08, 3.42178e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 1.18487e+08, 7.95618e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 3.36096e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 2.54409e+08, 1.1378e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 2.5777e+08, 0 }, { 3.35945e+08, 1.13433e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.41889e+07, 8.09077e+07, 8.31814e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.16899e+07, 7.06824e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51131e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 401512, 6.47115e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 3.72506e+08, 6.54585e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 3.56709e+07, 1.97605e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 3.36835e+08, 4.5698e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 273554, 4.7863e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 3.72233e+08, 6.54537e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 3.72506e+08, 0 }, { 1.00982e+08, 6.53552e+10 } } kg +compflowStatistics: Max phase CFL number: 1.2493 +compflowStatistics: Max component CFL number: 0.603237 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.87e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.42e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00267516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.028846 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.89817e+08s, dt:988365s, Cycle: 735 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.81e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.81e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.93e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00427999 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0475103 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.90805e+08s, dt:730653s, Cycle: 736 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.36e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00302066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0349044 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.91536e+08s, dt:1.09748e+06s, Cycle: 737 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.52e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.52e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00467899 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0567438 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.92633e+08s, dt:1.25606e+06s, Cycle: 738 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.16e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00582553 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0765155 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.9389e+08s, dt:1.18267e+06s, Cycle: 739 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00533367 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0776509 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.95072e+08s, dt:1.10235e+06s, Cycle: 740 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-04 ) ; + Last LinSolve(iter,res) = ( 3, 4.64e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00495532 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721131 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.96175e+08s, dt:1.0806e+06s, Cycle: 741 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.66e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.66e-07 ) ; + Last LinSolve(iter,res) = ( 5, 1.88e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.004787 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651952 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.97255e+08s, dt:1.13242e+06s, Cycle: 742 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.38e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.38e-05 ) ; + Last LinSolve(iter,res) = ( 9, 3.01e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00497531 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646049 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.98388e+08s, dt:1.19376e+06s, Cycle: 743 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.03e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.80e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00505541 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708827 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.99581e+08s, dt:1.1838e+06s, Cycle: 744 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00468494 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0713792 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.00765e+08s, dt:1.16846e+06s, Cycle: 745 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.61e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00417539 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665199 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.01934e+08s, dt:1.20851e+06s, Cycle: 746 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.59e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.59e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.25e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00432998 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0773033 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.03142e+08s, dt:1.12992e+06s, Cycle: 747 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.96e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00397043 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728416 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.04272e+08s, dt:1.10015e+06s, Cycle: 748 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.34e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.34e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.62e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00416856 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604664 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.05372e+08s, dt:1.21001e+06s, Cycle: 749 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-07 ) ; + Last LinSolve(iter,res) = ( 7, 3.40e-04 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00427029 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.096883 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.06582e+08s, dt:963362s, Cycle: 750 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00344959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664263 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.07546e+08s, dt:997305s, Cycle: 751 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.15e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00337418 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0501881 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.08543e+08s, dt:1.22925e+06s, Cycle: 752 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.06e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.06e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00409576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.104753 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.09772e+08s, dt:923563s, Cycle: 753 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.45e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.45e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00323854 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0905269 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.10696e+08s, dt:772537s, Cycle: 754 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.47e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.78e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.78e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00265305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0794581 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.11468e+08s, dt:708699s, Cycle: 755 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00238962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0711076 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.12177e+08s, dt:701301s, Cycle: 756 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.42e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.28e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.28e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00227499 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.12878e+08s, dt:743692s, Cycle: 757 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.95e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00245072 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0597419 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.13622e+08s, dt:824214s, Cycle: 758 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.23e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.84e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00278031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.075836 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.14446e+08s, dt:780816s, Cycle: 759 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.31e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.31e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.94e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.94e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.48e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0027251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0772065 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.15227e+08s, dt:730667s, Cycle: 760 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.27e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.34e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.34e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00250009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0720883 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.15958e+08s, dt:716419s, Cycle: 761 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.71e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.69e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.33e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0023345 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638395 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.16674e+08s, dt:761072s, Cycle: 762 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.04e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00260286 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0559511 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17435e+08s, dt:878632s, Cycle: 763 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.85e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.33e-04 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00321977 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681925 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.18314e+08s, dt:894022s, Cycle: 764 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.93e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00310132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0795558 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.19208e+08s, dt:819447s, Cycle: 765 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.04e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.55e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.55e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00285577 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753705 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.20027e+08s, dt:724845s, Cycle: 766 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.64e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00267748 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644808 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.20752e+08s, dt:765060s, Cycle: 767 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.66486e+07, 7.85635e+07, 7.99248e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.41503e+07, 6.74265e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.8097e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 333723, 6.77633e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 3.13518e+08, 6.85083e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.93416e+08, 2.0655e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 1.20102e+08, 4.78533e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 5.68122e+06, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 3.07837e+08, 6.85083e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 3.13518e+08, 0 }, { 4.40017e+08, 6.8054e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.61843e+07, 7.75811e+07, 7.84714e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.3686e+07, 6.59731e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33352e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 119980, 1.32152e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 1.12403e+08, 1.33621e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 6.23913e+07, 4.04545e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 5.00112e+07, 9.31664e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 966099, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 1.11436e+08, 1.33621e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 1.12403e+08, 0 }, { 1.3704e+08, 1.32204e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.38222e+07, 7.55386e+07, 7.7944e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.13239e+07, 6.54457e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35313e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.44427e+07, 1.10871e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.26553e+10, 1.12162e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 2.10332e+09, 4.1084e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.0552e+10, 7.10782e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 2.26006e+07, 4.00864e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.26327e+10, 1.08154e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.26553e+10, 0 }, { 2.10726e+09, 1.09988e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.75319e+07, 8.06596e+07, 8.23024e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.50336e+07, 6.98041e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12734e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 202984, 1.12531e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.9169e+08, 1.13851e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.35591e+08, 3.42178e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 5.60987e+07, 7.96336e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 4.98189e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.86708e+08, 1.13851e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.9169e+08, 0 }, { 3.97847e+08, 1.13441e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.41033e+07, 8.08212e+07, 8.30947e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.1605e+07, 7.05964e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51106e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 453089, 6.46575e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 4.20193e+08, 6.54054e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 3.84006e+07, 1.97604e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 3.81792e+08, 4.5645e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 206667, 4.78606e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 4.19986e+08, 6.54006e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 4.20193e+08, 0 }, { 1.27092e+08, 6.52753e+10 } } kg +compflowStatistics: Max phase CFL number: 1.07085 +compflowStatistics: Max component CFL number: 0.34083 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.74e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00323408 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613786 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.21517e+08s, dt:833497s, Cycle: 768 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00377789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0555663 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.22351e+08s, dt:721443s, Cycle: 769 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.32e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.32e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.87e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00338661 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0387347 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.23072e+08s, dt:1.02735e+06s, Cycle: 770 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00456874 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0391192 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.24099e+08s, dt:1.45539e+06s, Cycle: 771 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.19e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 3.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.71e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00529491 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588467 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.25555e+08s, dt:1.62835e+06s, Cycle: 772 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.48e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0052839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684889 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.27183e+08s, dt:1.65213e+06s, Cycle: 773 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.07e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00497626 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675913 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.28835e+08s, dt:1.69092e+06s, Cycle: 774 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.82e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00541362 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694575 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.30526e+08s, dt:1.6997e+06s, Cycle: 775 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.11e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.11e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.19e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00537927 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0605017 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.32226e+08s, dt:1.86875e+06s, Cycle: 776 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.29e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00567769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678788 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.34095e+08s, dt:1.90728e+06s, Cycle: 777 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.32e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.55e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.55e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.94e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0056088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684304 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.36002e+08s, dt:1.93622e+06s, Cycle: 778 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.02e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00544705 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068559 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.37938e+08s, dt:1.96316e+06s, Cycle: 779 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.23e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.23e-07 ) ; + Last LinSolve(iter,res) = ( 8, 1.41e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00561311 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.073631 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.39901e+08s, dt:1.89754e+06s, Cycle: 780 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.67e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00551026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070625 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.41799e+08s, dt:1.88632e+06s, Cycle: 781 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.80e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 9, 3.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 943158.4023806675 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.53e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.17e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00274385 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0370651 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 943158.4023806675, remaining dt = 943158.4023806675 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.70e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.70e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.16e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00281307 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0404445 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.43685e+08s, dt:1.31264e+06s, Cycle: 782 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 6, 3.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00403405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0608961 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.44998e+08s, dt:1.43726e+06s, Cycle: 783 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00435802 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688418 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.46435e+08s, dt:1.45329e+06s, Cycle: 784 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00435975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067424 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.47888e+08s, dt:1.48984e+06s, Cycle: 785 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.41e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.17e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00444443 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619523 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.49378e+08s, dt:1.6135e+06s, Cycle: 786 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.28e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.03e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00489564 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594127 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.50992e+08s, dt:1.29635e+06s, Cycle: 787 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.39e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00369356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0471549 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.52288e+08s, dt:1.65683e+06s, Cycle: 788 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.65782e+07, 7.84932e+07, 7.98543e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.40809e+07, 6.7357e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80949e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 282549, 6.78123e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 2.65393e+08, 6.85601e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.89884e+08, 2.06548e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 7.55097e+07, 4.79053e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 8.10273e+06, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 2.57291e+08, 6.85601e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 2.65393e+08, 0 }, { 4.67907e+08, 6.80771e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.61138e+07, 7.75107e+07, 7.84009e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.36165e+07, 6.59035e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33348e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 99419.8, 1.32353e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 9.3123e+07, 1.33832e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 6.12586e+07, 4.04546e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 3.18644e+07, 9.33771e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 1.89349e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 9.12295e+07, 1.33832e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 9.3123e+07, 0 }, { 1.44015e+08, 1.32343e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.37529e+07, 7.54681e+07, 7.78734e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.12555e+07, 6.53761e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35309e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.43456e+07, 1.10964e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.25588e+10, 1.12256e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 2.0981e+09, 4.10822e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.04607e+10, 7.11737e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 2.74967e+07, 4.00935e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.25313e+10, 1.08247e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.25588e+10, 0 }, { 2.13183e+09, 1.10056e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.74615e+07, 8.05894e+07, 8.22319e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.49641e+07, 6.97346e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.1273e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 175915, 1.12554e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.66104e+08, 1.13881e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.30813e+08, 3.42185e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 3.52902e+07, 7.96629e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 5.69787e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.60406e+08, 1.13881e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.66104e+08, 0 }, { 4.57579e+08, 1.1341e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.4034e+07, 8.07509e+07, 8.30243e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.15366e+07, 7.0527e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51086e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 497015, 6.46116e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 4.60812e+08, 6.53617e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.14628e+07, 1.97607e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 4.19349e+08, 4.5601e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 486361, 4.78577e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 4.60326e+08, 6.5357e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 4.60812e+08, 0 }, { 1.56833e+08, 6.52013e+10 } } kg +compflowStatistics: Max phase CFL number: 1.62037 +compflowStatistics: Max component CFL number: 0.445061 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-04 ) ; + Last LinSolve(iter,res) = ( 12, 4.76e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00480392 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0711312 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.53945e+08s, dt:663166s, Cycle: 789 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.22e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00175401 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0306096 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.54608e+08s, dt:1.06131e+06s, Cycle: 790 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.28e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.93e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00292841 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.053597 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.55669e+08s, dt:1.25781e+06s, Cycle: 791 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 9, 3.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-06 ) ; + Last LinSolve(iter,res) = ( 9, 2.18e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00362874 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637287 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.56927e+08s, dt:1.33771e+06s, Cycle: 792 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-06 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-04 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00376277 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623006 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.58265e+08s, dt:1.44356e+06s, Cycle: 793 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.65e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00378663 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594111 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.59708e+08s, dt:1.60546e+06s, Cycle: 794 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 7, 3.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.87e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00425556 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055703 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.61314e+08s, dt:1.85852e+06s, Cycle: 795 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.98e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.88e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00461417 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669018 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.63172e+08s, dt:1.91503e+06s, Cycle: 796 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.41e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.06e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00470736 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0748024 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.65087e+08s, dt:1.83127e+06s, Cycle: 797 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.17e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.17e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00456011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0705895 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.66919e+08s, dt:1.82105e+06s, Cycle: 798 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.47e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.47e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00471966 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633042 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.6874e+08s, dt:1.94509e+06s, Cycle: 799 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.66e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-04 ) ; + Last LinSolve(iter,res) = ( 10, 3.47e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00486377 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640441 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.70685e+08s, dt:2.06205e+06s, Cycle: 800 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.42e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00492028 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627959 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.72747e+08s, dt:2.21395e+06s, Cycle: 801 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 6, 2.95e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00528818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708501 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.74961e+08s, dt:2.19617e+06s, Cycle: 802 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.57e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.57e-06 ) ; + Last LinSolve(iter,res) = ( 5, 7.86e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00549205 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722442 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.77157e+08s, dt:2.15021e+06s, Cycle: 803 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 7, 3.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.74e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.74e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.61e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00560536 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627132 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.79307e+08s, dt:2.31056e+06s, Cycle: 804 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-01 ) ; + Last LinSolve(iter,res) = ( 16, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.36e-02 ) ; + Last LinSolve(iter,res) = ( 13, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.60e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.60e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00565845 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598266 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.81618e+08s, dt:2.20624e+06s, Cycle: 805 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.45e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00508724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645194 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.83824e+08s, dt:2.32e+06s, Cycle: 806 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.65161e+07, 7.84311e+07, 7.97921e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.40201e+07, 6.72961e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.8093e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 252754, 6.78403e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 2.37367e+08, 6.85903e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.84296e+08, 2.06547e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 5.30704e+07, 4.79356e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.38826e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 2.23484e+08, 6.85903e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 2.37367e+08, 0 }, { 4.93108e+08, 6.80815e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.60517e+07, 7.74486e+07, 7.83387e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.35557e+07, 6.58427e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33344e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 88043.5, 1.32464e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 8.24529e+07, 1.33946e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 5.97281e+07, 4.0454e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 2.27248e+07, 9.3492e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 998064, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 8.14549e+07, 1.33946e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 8.24529e+07, 0 }, { 1.48367e+08, 1.32412e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.36916e+07, 7.54059e+07, 7.78112e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.11956e+07, 6.53152e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35306e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.42403e+07, 1.11065e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.24558e+10, 1.12355e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 2.07657e+09, 4.10797e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.03792e+10, 7.12757e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 3.30351e+07, 4.01495e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.24228e+10, 1.0834e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.24558e+10, 0 }, { 2.13859e+09, 1.10149e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.73993e+07, 8.05274e+07, 8.21697e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.49033e+07, 6.96737e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12727e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 160200, 1.12567e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.51245e+08, 1.139e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.26537e+08, 3.42193e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 2.47073e+07, 7.9681e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 7.55865e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.43686e+08, 1.139e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.51245e+08, 0 }, { 5.1412e+08, 1.13371e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.39726e+07, 8.06889e+07, 8.29621e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.14766e+07, 7.04662e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51068e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 527942, 6.45789e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 4.89385e+08, 6.53328e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.31269e+07, 1.97615e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 4.46258e+08, 4.55713e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 436483, 4.78553e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 4.88948e+08, 6.5328e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 4.89385e+08, 0 }, { 1.9193e+08, 6.51363e+10 } } kg +compflowStatistics: Max phase CFL number: 1.67597 +compflowStatistics: Max component CFL number: 0.617532 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00522734 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0712351 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.86144e+08s, dt:2.29303e+06s, Cycle: 807 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.48e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.65e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00494496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0693331 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.88437e+08s, dt:2.30768e+06s, Cycle: 808 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 9, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.69e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00515592 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673177 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.90745e+08s, dt:2.36818e+06s, Cycle: 809 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.42e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.42e-06 ) ; + Last LinSolve(iter,res) = ( 8, 4.25e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00500587 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722627 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.93113e+08s, dt:2.31822e+06s, Cycle: 810 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.41e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.41e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.07e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00468263 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0709704 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.95431e+08s, dt:2.297e+06s, Cycle: 811 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.96e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00464524 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067846 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.97728e+08s, dt:2.3451e+06s, Cycle: 812 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00511676 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618958 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.00073e+08s, dt:2.54124e+06s, Cycle: 813 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.57e-03 ) ; + Line search @ 0.352: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.176: ( Rflow ) = ( 8.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.088: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 9, 3.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.82e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.82e-05 ) ; + Last LinSolve(iter,res) = ( 10, 1.50e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00575764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737767 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.02614e+08s, dt:2.45301e+06s, Cycle: 814 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.48e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.89e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00541104 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722533 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.05067e+08s, dt:2.40148e+06s, Cycle: 815 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.19e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.19e-07 ) ; + Last LinSolve(iter,res) = ( 6, 2.48e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00496544 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655844 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.07469e+08s, dt:2.5069e+06s, Cycle: 816 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-03 ) ; + Last LinSolve(iter,res) = ( 10, 3.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 10, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 10, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1253451.1308274348 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.12e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.63e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00253764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0348589 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1253451.1308274348, remaining dt = 1253451.1308274348 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 2.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.37e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.85e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00253817 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0357029 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.09976e+08s, dt:1.86148e+06s, Cycle: 817 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.87e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.87e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.67e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00399379 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0533542 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.11837e+08s, dt:2.21219e+06s, Cycle: 818 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-01 ) ; + Last LinSolve(iter,res) = ( 6, 3.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.68e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00468104 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621887 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.1405e+08s, dt:1.31048e+06s, Cycle: 819 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-05 ) ; + Last LinSolve(iter,res) = ( 10, 5.28e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00265137 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0361808 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.1536e+08s, dt:1.93311e+06s, Cycle: 820 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.64626e+07, 7.83776e+07, 7.97385e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.39648e+07, 6.72407e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80914e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 232295, 6.78592e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 2.1812e+08, 6.86113e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.77804e+08, 2.06547e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 4.03158e+07, 4.79566e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.11024e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 2.07017e+08, 6.86113e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 2.1812e+08, 0 }, { 5.15681e+08, 6.80793e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.59982e+07, 7.73951e+07, 7.82851e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.35003e+07, 6.57872e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33341e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 80866.4, 1.32532e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 7.57201e+07, 1.34015e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 5.85612e+07, 4.04526e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 1.71588e+07, 9.35624e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 2.70371e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 7.30164e+07, 1.34015e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 7.57201e+07, 0 }, { 1.50635e+08, 1.32458e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.3639e+07, 7.53524e+07, 7.77576e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.11411e+07, 6.52597e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35302e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.41524e+07, 1.1115e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.23699e+10, 1.12435e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 2.05111e+09, 4.10765e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.03188e+10, 7.13585e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 3.91675e+07, 4.00977e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.23308e+10, 1.08425e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.23699e+10, 0 }, { 2.12816e+09, 1.1024e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.73458e+07, 8.0474e+07, 8.21162e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.48479e+07, 6.96183e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12725e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 149511, 1.12575e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.41138e+08, 1.13914e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.22474e+08, 3.42203e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 1.86638e+07, 7.96941e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 7.45746e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.3368e+08, 1.13914e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.41138e+08, 0 }, { 5.66843e+08, 1.13331e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.392e+07, 8.06355e+07, 8.29086e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.1422e+07, 7.04107e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51053e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 543378, 6.4562e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 5.03605e+08, 6.5321e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.3987e+07, 1.97627e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 4.59618e+08, 4.55583e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 749590, 4.7854e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 5.02855e+08, 6.53162e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 5.03605e+08, 0 }, { 2.32528e+08, 6.50829e+10 } } kg +compflowStatistics: Max phase CFL number: 1.06991 +compflowStatistics: Max component CFL number: 0.518529 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.89e-03 ) ; + Line search @ 0.257: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.128: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.064: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00393978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0490848 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.17293e+08s, dt:386891s, Cycle: 821 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-04 ) ; + Last LinSolve(iter,res) = ( 3, 3.62e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.000743062 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00960519 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.1768e+08s, dt:773782s, Cycle: 822 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.47e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.09e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0015061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0193234 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.18454e+08s, dt:1.49562e+06s, Cycle: 823 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.90e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.90e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.74e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00296056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0385028 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.19949e+08s, dt:2.13652e+06s, Cycle: 824 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.35e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00413799 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055525 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.22086e+08s, dt:2.47815e+06s, Cycle: 825 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.37e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.45e-03 ) ; + Line search @ 0.426: ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.213: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.107: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.15e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00469488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627498 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.24564e+08s, dt:2.66195e+06s, Cycle: 826 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.99e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00513171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623722 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.27226e+08s, dt:2.87048e+06s, Cycle: 827 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.29e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.07e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00561629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599509 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.30097e+08s, dt:3.17428e+06s, Cycle: 828 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.78e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Line search @ 0.496: ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.248: ( Rflow ) = ( 9.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.124: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.29e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.29e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.31e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00636074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064286 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.33271e+08s, dt:3.35696e+06s, Cycle: 829 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.96e-01 ) ; + Last LinSolve(iter,res) = ( 8, 3.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.43e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.00e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00637466 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675374 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.36628e+08s, dt:3.43758e+06s, Cycle: 830 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-05 ) ; + Last LinSolve(iter,res) = ( 13, 1.55e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00687819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066572 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.40065e+08s, dt:3.5536e+06s, Cycle: 831 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.69e-01 ) ; + Last LinSolve(iter,res) = ( 12, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-01 ) ; + Last LinSolve(iter,res) = ( 9, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.71e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.98e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.38e-01 ) ; + Last LinSolve(iter,res) = ( 11, 4.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.99e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.42e-03 ) ; + Line search @ 0.387: ( Rflow ) = ( 4.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.193: ( Rflow ) = ( 3.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.097: ( Rflow ) = ( 2.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.048: ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1776799.9035694592 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.54e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.22e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00348633 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0347453 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1776799.9035694592, remaining dt = 1776799.9035694592 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.65e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00334774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0347706 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.43619e+08s, dt:2.67396e+06s, Cycle: 832 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.19e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.58e-03 ) ; + Line search @ 0.393: ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.197: ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.098: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.36e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.91e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00481315 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0520824 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.46293e+08s, dt:603107s, Cycle: 833 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.56e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.56e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.47e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00105685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0119534 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.46896e+08s, dt:1.20621e+06s, Cycle: 834 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.6414e+07, 7.83288e+07, 7.96897e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.39148e+07, 6.71906e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.809e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 217174, 6.78728e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 2.03892e+08, 6.86268e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.72068e+08, 2.06547e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 3.18237e+07, 4.79721e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.14626e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.92429e+08, 6.86268e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 2.03892e+08, 0 }, { 5.36036e+08, 6.80739e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.59496e+07, 7.73463e+07, 7.82363e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.34504e+07, 6.57371e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33338e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 75196, 1.32586e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 7.04007e+07, 1.34068e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 5.67878e+07, 4.04511e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 1.36129e+07, 9.36167e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 2.51027e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 6.78904e+07, 1.34068e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 7.04007e+07, 0 }, { 1.5197e+08, 1.32497e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.35908e+07, 7.53037e+07, 7.77087e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.10916e+07, 6.52096e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35299e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.40651e+07, 1.11234e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.2285e+10, 1.12513e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 2.02e+09, 4.10731e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.0265e+10, 7.144e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 4.87883e+07, 4.02056e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.22362e+10, 1.08493e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.2285e+10, 0 }, { 2.10973e+09, 1.10338e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.72971e+07, 8.04253e+07, 8.20674e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.47979e+07, 6.95682e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12722e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 140787, 1.12581e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.32889e+08, 1.13927e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.18231e+08, 3.42212e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 1.46579e+07, 7.97053e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 6.99219e+06, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.25897e+08, 1.13927e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.32889e+08, 0 }, { 6.16711e+08, 1.13292e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.38717e+07, 8.05869e+07, 8.28598e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.13725e+07, 7.03607e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.5104e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 560026, 6.45439e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 5.18952e+08, 6.5309e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.504e+07, 1.97642e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 4.73912e+08, 4.55448e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 418303, 5.51771e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 5.18534e+08, 6.53035e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 5.18952e+08, 0 }, { 2.76784e+08, 6.50255e+10 } } kg +compflowStatistics: Max phase CFL number: 0.499515 +compflowStatistics: Max component CFL number: 0.324204 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00221217 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0244427 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.48102e+08s, dt:1.11379e+06s, Cycle: 835 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00201154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0229727 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.49216e+08s, dt:2.01728e+06s, Cycle: 836 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.38e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00360237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0424498 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.51233e+08s, dt:2.73487e+06s, Cycle: 837 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.85e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 9, 3.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.44e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.50e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.53e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.53e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 8.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.53e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1367432.8719873098 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0024565 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0291373 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1367432.8719873098, remaining dt = 1367432.8719873098 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0026167 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0292179 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.53968e+08s, dt:2.23583e+06s, Cycle: 838 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.86e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.96e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.96e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.59e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00404905 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.046962 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.56204e+08s, dt:2.86428e+06s, Cycle: 839 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00524734 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0589962 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.59068e+08s, dt:3.19959e+06s, Cycle: 840 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1599796.5602156164 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.17e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.36e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00293558 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0320057 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1599796.5602156164, remaining dt = 1599796.5602156164 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.23e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00278345 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0307902 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.62268e+08s, dt:2.55325e+06s, Cycle: 841 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.39e-03 ) ; + Line search @ 0.260: ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.130: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.065: ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.033: ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.46e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00491516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0450067 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.64821e+08s, dt:3.35085e+06s, Cycle: 842 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.80e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.80e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 9.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1675426.94206685 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.17e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00285505 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0307685 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1675426.94206685, remaining dt = 1675426.94206685 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.79e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00283897 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0327594 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.68172e+08s, dt:2.59624e+06s, Cycle: 843 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.15e-03 ) ; + Line search @ 0.186: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.093: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.047: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.17e-03 ) ; + Line search @ 0.058: ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.029: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.015: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.007: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.73e-02 ) ; + Last LinSolve(iter,res) = ( 11, 3.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.31e-02 ) ; + Last LinSolve(iter,res) = ( 11, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.70e-02 ) ; + Last LinSolve(iter,res) = ( 11, 3.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.74e-02 ) ; + Last LinSolve(iter,res) = ( 11, 3.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.52e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.35e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 8.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.46e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 8.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.30e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 1298120.6043199934 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.07e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00218629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0259176 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1298120.6043199934, remaining dt = 1298120.6043199934 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.22e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00216048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0265008 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.70768e+08s, dt:2.21628e+06s, Cycle: 844 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.78e-03 ) ; + Line search @ 0.056: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.028: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.014: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.11e-03 ) ; + Line search @ 0.013: ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.007: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.003: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.002: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.22e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.22e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00407514 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0451618 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.72984e+08s, dt:2.90299e+06s, Cycle: 845 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-04 ) ; + Last LinSolve(iter,res) = ( 10, 5.49e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00472796 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0718261 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.75887e+08s, dt:2.54454e+06s, Cycle: 846 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.13e-03 ) ; + Last LinSolve(iter,res) = ( 10, 4.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.47e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00426215 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604455 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.78432e+08s, dt:2.32e+06s, Cycle: 847 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.63694e+07, 7.82842e+07, 7.9645e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.38729e+07, 6.71485e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80887e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 205670, 6.7883e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 1.93067e+08, 6.86385e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.67171e+08, 2.06547e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 2.58953e+07, 4.79838e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.3232e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.79835e+08, 6.86385e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 1.93067e+08, 0 }, { 5.53824e+08, 6.80674e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.5905e+07, 7.73016e+07, 7.81916e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.34085e+07, 6.5695e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33335e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 70558.8, 1.3263e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 6.60506e+07, 1.34108e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 5.5125e+07, 4.04491e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 1.09256e+07, 9.36594e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 3.76131e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 6.22893e+07, 1.34108e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 6.60506e+07, 0 }, { 1.52099e+08, 1.32537e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.35468e+07, 7.52592e+07, 7.7664e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.10502e+07, 6.51675e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35297e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.39835e+07, 1.11313e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.22058e+10, 1.12585e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.98067e+09, 4.10696e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.02251e+10, 7.15153e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 4.31649e+07, 4.0361e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.21626e+10, 1.08549e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.22058e+10, 0 }, { 2.08531e+09, 1.10435e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.72525e+07, 8.03807e+07, 8.20227e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.47559e+07, 6.95262e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.1272e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 133897, 1.12586e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.26375e+08, 1.13937e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.14709e+08, 3.42222e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 1.16653e+07, 7.97146e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 1.00528e+07, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.16322e+08, 1.13937e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.26375e+08, 0 }, { 6.63811e+08, 1.13254e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.38277e+07, 8.05424e+07, 8.28152e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.13311e+07, 7.03186e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51027e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 573992, 6.45287e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 5.31818e+08, 6.53005e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.56296e+07, 1.97659e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 4.86188e+08, 4.55346e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 883456, 5.5175e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 5.30935e+08, 6.5295e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 5.31818e+08, 0 }, { 3.24204e+08, 6.49684e+10 } } kg +compflowStatistics: Max phase CFL number: 0.736092 +compflowStatistics: Max component CFL number: 0.621932 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.18e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.42e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00409969 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0543846 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.80752e+08s, dt:2.7253e+06s, Cycle: 848 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.42e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00461846 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648504 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.83477e+08s, dt:2.86585e+06s, Cycle: 849 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00510941 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689455 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.86343e+08s, dt:2.89493e+06s, Cycle: 850 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.55e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00515817 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644186 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.89238e+08s, dt:3.05745e+06s, Cycle: 851 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-01 ) ; + Last LinSolve(iter,res) = ( 9, 3.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-01 ) ; + Last LinSolve(iter,res) = ( 8, 3.44e-03 ) ; + Line search @ 0.481: ( Rflow ) = ( 3.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.240: ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.120: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.060: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00511658 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0615736 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.92296e+08s, dt:3.32422e+06s, Cycle: 852 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.45e-01 ) ; + Last LinSolve(iter,res) = ( 7, 3.86e-03 ) ; + Line search @ 0.480: ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.240: ( Rflow ) = ( 9.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.120: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00528001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0610524 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.9562e+08s, dt:3.63388e+06s, Cycle: 853 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 1816941.0928808632 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.01e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.61e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00286449 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0342553 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1816941.0928808632, remaining dt = 1816941.0928808632 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 3.30e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00289262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0359264 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.99254e+08s, dt:2.68981e+06s, Cycle: 854 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.52e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 10, 3.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.03e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00465079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0540596 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.01943e+08s, dt:3.17125e+06s, Cycle: 855 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; + Line search @ 0.243: ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.121: ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.061: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.030: ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.27e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.32e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.34e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.35e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.35e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.36e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.36e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.34e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1585626.0559663377 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.92e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.14e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00257467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0319664 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1585626.0559663377, remaining dt = 1585626.0559663377 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00252005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0314927 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.05115e+08s, dt:2.5039e+06s, Cycle: 856 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 9, 3.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.98e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.98e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.21e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00461359 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0456819 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.07619e+08s, dt:2.3494e+06s, Cycle: 857 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.98e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.98e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00374063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0497161 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.09968e+08s, dt:2.32e+06s, Cycle: 858 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.63269e+07, 7.82416e+07, 7.96024e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.383e+07, 6.71055e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80874e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 195569, 6.78918e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 1.83562e+08, 6.86485e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.61865e+08, 2.06546e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 2.16969e+07, 4.79939e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.10615e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.725e+08, 6.86485e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 1.83562e+08, 0 }, { 5.69453e+08, 6.80614e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.58626e+07, 7.72591e+07, 7.8149e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.33656e+07, 6.5652e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33333e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 66318.6, 1.3267e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 6.2074e+07, 1.34144e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 5.30423e+07, 4.04466e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 9.03168e+06, 9.3697e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 2.86376e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 5.92103e+07, 1.34144e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 6.2074e+07, 0 }, { 1.51243e+08, 1.32581e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.35049e+07, 7.52168e+07, 7.76214e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.10079e+07, 6.51245e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35294e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.39064e+07, 1.11388e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.2131e+10, 1.12652e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.94617e+09, 4.1066e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.01848e+10, 7.15861e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 4.43914e+07, 4.04634e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.20866e+10, 1.08606e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.2131e+10, 0 }, { 2.0595e+09, 1.1053e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.721e+07, 8.03382e+07, 8.19802e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.4713e+07, 6.94832e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12718e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 128142, 1.1259e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.20933e+08, 1.13946e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.11476e+08, 3.42232e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 9.45784e+06, 7.97227e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 1.0565e+07, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.10368e+08, 1.13946e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.20933e+08, 0 }, { 7.09307e+08, 1.13217e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.37857e+07, 8.05e+07, 8.27734e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.12887e+07, 7.02764e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51015e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 585100, 6.45164e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 5.42036e+08, 6.52954e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.59556e+07, 1.97678e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 4.9608e+08, 4.55276e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 799188, 5.51719e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 5.41237e+08, 6.52899e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 5.42036e+08, 0 }, { 3.7324e+08, 6.49129e+10 } } kg +compflowStatistics: Max phase CFL number: 0.638921 +compflowStatistics: Max component CFL number: 0.622003 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 10, 4.38e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00361959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0489133 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.12288e+08s, dt:2.903e+06s, Cycle: 859 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0046123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0580453 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.15191e+08s, dt:3.27598e+06s, Cycle: 860 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.61e-03 ) ; + Line search @ 0.395: ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.198: ( Rflow ) = ( 8.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.099: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.77e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00543854 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0595087 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.18467e+08s, dt:3.63964e+06s, Cycle: 861 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.04e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.87e-03 ) ; + Line search @ 0.225: ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.113: ( Rflow ) = ( 9.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.056: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.93e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.92e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00555214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674419 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.22107e+08s, dt:3.73053e+06s, Cycle: 862 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.30e-01 ) ; + Last LinSolve(iter,res) = ( 15, 4.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e+00 ) ; + Last LinSolve(iter,res) = ( 15, 9.27e-03 ) ; + Line search @ 0.486: ( Rflow ) = ( 5.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.243: ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.121: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.061: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 16, 3.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 10, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e+00 ) ; + Last LinSolve(iter,res) = ( 16, 2.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.22e-01 ) ; + Last LinSolve(iter,res) = ( 15, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 15, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.39e-01 ) ; + Last LinSolve(iter,res) = ( 16, 2.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 14, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 9.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.78e-01 ) ; + Last LinSolve(iter,res) = ( 16, 3.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 11, 4.85e-03 ) ; +New dt = 1865265.8061515102 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.76e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.76e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.60e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00276477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0357271 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1865265.8061515102, remaining dt = 1865265.8061515102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.74e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.11e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00280885 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0357868 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.25837e+08s, dt:2.7668e+06s, Cycle: 863 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 12, 4.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.29e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00449439 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0496897 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.28604e+08s, dt:3.43033e+06s, Cycle: 864 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 11, 3.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00574538 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0519649 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.32034e+08s, dt:4.14173e+06s, Cycle: 865 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.96e-01 ) ; + Last LinSolve(iter,res) = ( 9, 3.56e-03 ) ; + Line search @ 0.331: ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.166: ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.083: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.041: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.50e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.50e-07 ) ; + Last LinSolve(iter,res) = ( 5, 1.84e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00649978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593457 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.36176e+08s, dt:4.60945e+06s, Cycle: 866 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.73e-07 ) ; + Last LinSolve(iter,res) = ( 5, 1.51e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00667381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069671 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.40785e+08s, dt:718537s, Cycle: 867 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.26e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00101475 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0108732 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.41504e+08s, dt:1.43707e+06s, Cycle: 868 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.62877e+07, 7.82023e+07, 7.95631e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.37885e+07, 6.70639e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80862e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 187123, 6.78991e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 1.75614e+08, 6.86565e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.57197e+08, 2.06544e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 1.84172e+07, 4.80021e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.0083e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.65531e+08, 6.86565e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 1.75614e+08, 0 }, { 5.81701e+08, 6.80568e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.58233e+07, 7.72197e+07, 7.81096e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.33241e+07, 6.56105e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33331e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 62830.7, 1.32702e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 5.88033e+07, 1.34169e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 5.13186e+07, 4.04435e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 7.48469e+06, 9.37256e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 2.95503e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 5.58482e+07, 1.34169e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 5.88033e+07, 0 }, { 1.49078e+08, 1.32629e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.34659e+07, 7.51776e+07, 7.75821e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.09668e+07, 6.50829e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.35292e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.3838e+07, 1.11454e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.20645e+10, 1.1271e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.91113e+09, 4.10624e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.01534e+10, 7.16479e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 4.69147e+07, 4.06367e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.20176e+10, 1.08647e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.20645e+10, 0 }, { 2.03051e+09, 1.10619e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.71707e+07, 8.02989e+07, 8.19408e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.46715e+07, 6.94417e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12716e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 123501, 1.12593e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.16543e+08, 1.13954e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.08807e+08, 3.42242e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 7.73645e+06, 7.97298e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 1.45039e+07, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 1.02039e+08, 1.13954e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.16543e+08, 0 }, { 7.53585e+08, 1.13179e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.37467e+07, 8.04608e+07, 8.27348e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.12475e+07, 7.02356e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.51004e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 591048, 6.45093e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 5.47476e+08, 6.52961e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.62713e+07, 1.97698e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 5.01205e+08, 4.55263e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 930613, 5.51685e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 5.46545e+08, 6.52906e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 5.47476e+08, 0 }, { 4.24532e+08, 6.4861e+10 } } kg +compflowStatistics: Max phase CFL number: 0.341137 +compflowStatistics: Max component CFL number: 0.383755 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.05e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.62e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0020509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0221333 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.42941e+08s, dt:882925s, Cycle: 869 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.12e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.26e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00124814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0138008 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.43824e+08s, dt:1.76585e+06s, Cycle: 870 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.60e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.60e-07 ) ; + Last LinSolve(iter,res) = ( 6, 2.42e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00250564 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0287473 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.4559e+08s, dt:2.90858e+06s, Cycle: 871 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.83e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.59e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0042594 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0475046 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.48498e+08s, dt:3.70163e+06s, Cycle: 872 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.63e-03 ) ; + Line search @ 0.079: ( Rflow ) = ( 4.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.039: ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.020: ( Rflow ) = ( 2.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.010: ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.78e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.78e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00565177 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0559099 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.522e+08s, dt:4.27534e+06s, Cycle: 873 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 2137669.6215701792 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.90e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00301081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0367232 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 2137669.6215701792, remaining dt = 2137669.6215701792 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.48e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.40e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.40e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.20e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00302875 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0384577 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.56475e+08s, dt:3.05557e+06s, Cycle: 874 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.17e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00443618 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0577179 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.59531e+08s, dt:3.46033e+06s, Cycle: 875 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.88e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.00e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.00e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00529025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664193 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.62991e+08s, dt:3.5825e+06s, Cycle: 876 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 10, 5.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 1791251.6682528993 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.46e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.46e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.73e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0024813 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0343775 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1791251.6682528993, remaining dt = 1791251.6682528993 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.69e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00251888 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0335341 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.66574e+08s, dt:2.74435e+06s, Cycle: 877 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 10, 3.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 11, 2.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.24e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 9, 4.43e-03 ) ; +New dt = 1372173.7894767658 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.83e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.96e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.96e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00195434 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0248484 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1372173.7894767658, remaining dt = 1372173.7894767658 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00200833 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0236649 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.69318e+08s, dt:2.45595e+06s, Cycle: 878 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-01 ) ; + Last LinSolve(iter,res) = ( 14, 3.31e-03 ) ; + Line search @ 0.234: ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.117: ( Rflow ) = ( 2.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.058: ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.029: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 10, 4.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-04 ) ; + Last LinSolve(iter,res) = ( 10, 5.53e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00378675 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.037122 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.71774e+08s, dt:1.26589e+06s, Cycle: 879 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00190553 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.018008 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.7304e+08s, dt:2.32e+06s, Cycle: 880 +compflowStatistics, Reservoir: Pressure (min, average, max): 7.62508e+07, 7.81653e+07, 7.95261e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 6.37523e+07, 6.70276e+07 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Reservoir: Total dynamic pore volume: 6.80851e+07 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 180042, 6.79051e+07 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 1.68951e+08, 6.86625e+10 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 1.53404e+08, 2.0654e+10 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 1.55475e+07, 4.80085e+10 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 1.293e+07, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.56021e+08, 6.86625e+10 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 1.68951e+08, 0 }, { 5.90248e+08, 6.80542e+10 } } kg +compflowStatistics, Caprock: Pressure (min, average, max): 7.57864e+07, 7.71828e+07, 7.80727e+07 Pa +compflowStatistics, Caprock: Delta pressure (min, max): 6.32879e+07, 6.55742e+07 Pa +compflowStatistics, Caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Caprock: Total dynamic pore volume: 1.33329e+07 rm^3 +compflowStatistics, Caprock: Phase dynamic pore volumes: { 59834.5, 1.3273e+07 } rm^3 +compflowStatistics, Caprock: Phase mass: { 5.59937e+07, 1.34189e+10 } kg +compflowStatistics, Caprock: Trapped phase mass (metric 1): { 4.97379e+07, 4.04402e+09 } kg +compflowStatistics, Caprock: Non-trapped phase mass (metric 1): { 6.25578e+06, 9.37486e+09 } kg +compflowStatistics, Caprock: Immobile phase mass (metric 2): { 3.6646e+06, 0 } kg +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 5.23291e+07, 1.34189e+10 } kg +compflowStatistics, Caprock: Dissolved component mass: { { 5.59937e+07, 0 }, { 1.4628e+08, 1.32678e+10 } } kg +compflowStatistics, Overburden: Pressure (min, average, max): 7.34293e+07, 7.51408e+07, 7.75452e+07 Pa +compflowStatistics, Overburden: Delta pressure (min, max): 6.09308e+07, 6.50467e+07 Pa +compflowStatistics, Overburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Overburden: Total dynamic pore volume: 1.3529e+08 rm^3 +compflowStatistics, Overburden: Phase dynamic pore volumes: { 2.37747e+07, 1.11515e+08 } rm^3 +compflowStatistics, Overburden: Phase mass: { 2.2003e+10, 1.12763e+11 } kg +compflowStatistics, Overburden: Trapped phase mass (metric 1): { 1.8749e+09, 4.10589e+10 } kg +compflowStatistics, Overburden: Non-trapped phase mass (metric 1): { 2.01281e+10, 7.17045e+10 } kg +compflowStatistics, Overburden: Immobile phase mass (metric 2): { 4.03503e+07, 4.07034e+09 } kg +compflowStatistics, Overburden: Mobile phase mass (metric 2): { 2.19626e+10, 1.08693e+11 } kg +compflowStatistics, Overburden: Dissolved component mass: { { 2.2003e+10, 0 }, { 2.00016e+09, 1.10704e+11 } } kg +compflowStatistics, Underburden: Pressure (min, average, max): 7.71338e+07, 8.0262e+07, 8.19039e+07 Pa +compflowStatistics, Underburden: Delta pressure (min, max): 6.46353e+07, 6.94054e+07 Pa +compflowStatistics, Underburden: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Underburden: Total dynamic pore volume: 1.12714e+08 rm^3 +compflowStatistics, Underburden: Phase dynamic pore volumes: { 118830, 1.12595e+08 } rm^3 +compflowStatistics, Underburden: Phase mass: { 1.12128e+08, 1.13962e+11 } kg +compflowStatistics, Underburden: Trapped phase mass (metric 1): { 1.05653e+08, 3.42252e+10 } kg +compflowStatistics, Underburden: Non-trapped phase mass (metric 1): { 6.47496e+06, 7.97371e+10 } kg +compflowStatistics, Underburden: Immobile phase mass (metric 2): { 1.71757e+07, 0 } kg +compflowStatistics, Underburden: Mobile phase mass (metric 2): { 9.49522e+07, 1.13962e+11 } kg +compflowStatistics, Underburden: Dissolved component mass: { { 1.12128e+08, 0 }, { 7.97355e+08, 1.13143e+11 } } kg +compflowStatistics, Salt: Pressure (min, average, max): 7.37101e+07, 8.0424e+07, 8.26983e+07 Pa +compflowStatistics, Salt: Delta pressure (min, max): 6.12116e+07, 7.01998e+07 Pa +compflowStatistics, Salt: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, Salt: Total dynamic pore volume: 6.50993e+07 rm^3 +compflowStatistics, Salt: Phase dynamic pore volumes: { 594873, 6.45045e+07 } rm^3 +compflowStatistics, Salt: Phase mass: { 5.50952e+08, 6.52994e+10 } kg +compflowStatistics, Salt: Trapped phase mass (metric 1): { 4.62545e+07, 1.9772e+10 } kg +compflowStatistics, Salt: Non-trapped phase mass (metric 1): { 5.04698e+08, 4.55275e+10 } kg +compflowStatistics, Salt: Immobile phase mass (metric 2): { 1.39034e+06, 5.51655e+06 } kg +compflowStatistics, Salt: Mobile phase mass (metric 2): { 5.49562e+08, 6.52939e+10 } kg +compflowStatistics, Salt: Dissolved component mass: { { 5.50952e+08, 0 }, { 4.77311e+08, 6.48101e+10 } } kg +compflowStatistics: Max phase CFL number: 0.509797 +compflowStatistics: Max component CFL number: 0.619342 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 7, 3.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.62e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.62e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.47e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00344662 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0334972 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.7536e+08s, dt:3.55635e+06s, Cycle: 881 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.95e-01 ) ; + Last LinSolve(iter,res) = ( 10, 5.87e-03 ) ; + Line search @ 0.295: ( Rflow ) = ( 4.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.148: ( Rflow ) = ( 3.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.074: ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.037: ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.98e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00538232 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0533194 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.78916e+08s, dt:4.22802e+06s, Cycle: 882 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.23e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00573902 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691063 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.83144e+08s, dt:4.26432e+06s, Cycle: 883 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.44e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00627736 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061967 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.87409e+08s, dt:4.61758e+06s, Cycle: 884 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.10e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; +New dt = 2308792.268887146 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.47e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.47e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.003035 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0328496 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 2308792.268887146, remaining dt = 2308792.268887146 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.20e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00298645 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0316684 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.92026e+08s, dt:3.63626e+06s, Cycle: 885 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-01 ) ; + Last LinSolve(iter,res) = ( 7, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.95e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.38e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 7, 3.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.91e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; +New dt = 1818127.579971809 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-02 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.14e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00232021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0240475 +coupledFlowAndWells: Time-step required will be increased based on state change. +coupledFlowAndWells: sub-step = 0, accepted dt = 1818127.579971809, remaining dt = 1818127.579971809 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 6, 2.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.97e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.97e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.91e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00240054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0229461 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.95663e+08s, dt:3.2945e+06s, Cycle: 886 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.70e-01 ) ; + Last LinSolve(iter,res) = ( 8, 4.87e-03 ) ; + Line search @ 0.227: ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.113: ( Rflow ) = ( 2.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.057: ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.028: ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.15e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00415563 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.041186 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.98957e+08s, dt:1.04297e+06s, Cycle: 887 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; +wellControls1: well is shut +wellControls2: well is shut +wellControls3: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00128732 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0131013 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Cleaning up events +Umpire HOST sum across ranks: 164.1 MB +Umpire HOST rank max: 164.1 MB +Finished at 2023-06-20 16:50:29 +total time 00:45:34.246 +initialization time 00:11:31.716 +run time 00:33:58.393 diff --git a/geos-posp/tests/Data/job_GEOS_891567.out b/geos-posp/tests/Data/job_GEOS_891567.out new file mode 100644 index 00000000..1472d00d --- /dev/null +++ b/geos-posp/tests/Data/job_GEOS_891567.out @@ -0,0 +1,133436 @@ +GEOSX version: 0.2.0 (HEAD, sha1: 2e19665) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, mesh +Adding Mesh: InternalWell, well_1 +Adding Event: PeriodicEvent, time_steps_1_output +Adding Event: PeriodicEvent, time_steps_1_applications +Adding Event: PeriodicEvent, time_steps_2_output +Adding Event: PeriodicEvent, time_steps_2_applications +Adding Event: PeriodicEvent, statistics +Adding Output: VTK, hexdom_well_module_multiphaseWell + TableFunction: totalRateTable +Adding Object CellElementRegion named caprock from ObjectManager::Catalog. +Adding Object CellElementRegion named reservoir from ObjectManager::Catalog. +Adding Object WellElementRegion named well_1region from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: well_1Control_ConstantBHP_table + TableFunction: well_1Control_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table +VTKMesh 'mesh': reading mesh from /work206/workrd/users/l1045328/job_GEOS/maillage_tresfin/TPFA/Wtrue/hexdom_Wtrue.vtu + reading the dataset... + redistributing mesh... +Generating global Ids from VTK mesh + finding neighbor ranks... + done! +VTKMesh 'mesh': generating GEOSX mesh data structure + preprocessing... + writing nodes... + writing cells... +Importing cell block 3_tetrahedra +Importing cell block 1_tetrahedra +Importing cell block 2_tetrahedra +Importing cell block 3_pyramids +Importing cell block 1_pyramids +Importing cell block 2_pyramids +Importing cell block 2_hexahedra +Importing cell block 3_hexahedra +Importing cell block 1_hexahedra + writing surfaces... +Importing surface 2 +Importing surface 3 +Importing surface 1 + building connectivity maps... + done! +Number of nodes: 2558433 + Number of elems: 3021450 + Polygon: 210306 + C3D4: 304106 + C3D5: 67546 + C3D8: 2439492 +Load balancing: min avg max +(element/rank): 4072 5901 6196 +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_hexahedra +mesh/Level0/caprock/1_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_hexahedra/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_pyramids +mesh/Level0/caprock/1_pyramids/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_pyramids/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_tetrahedra +mesh/Level0/caprock/1_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_tetrahedra/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_hexahedra +mesh/Level0/reservoir/2_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_pyramids +mesh/Level0/reservoir/2_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_tetrahedra +mesh/Level0/reservoir/2_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_hexahedra +mesh/Level0/reservoir/3_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_pyramids +mesh/Level0/reservoir/3_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_tetrahedra +mesh/Level0/reservoir/3_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, well_1region, well_1regionUniqueSubRegion +mesh/Level0/well_1region/well_1regionUniqueSubRegion/fluid allocated 1 quadrature points +mesh/Level0/well_1region/well_1regionUniqueSubRegion/relperm allocated 1 quadrature points +mesh/Level0/well_1region/well_1regionUniqueSubRegion/rockPermregion0 allocated 1 quadrature points +mesh: importing field data from mesh dataset +Time: 0s, dt:100s, Cycle: 0 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 1.98e+01 ) ; ( R ) = ( 1.98e+01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 1.04e-01 ) ; ( R ) = ( 2.78e-01 ) ; + Last LinSolve(iter,res) = ( 1, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 1.84e-02 ) ; ( R ) = ( 9.98e-02 ) ; + Last LinSolve(iter,res) = ( 2, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.50e-03 ) ; ( Rwell ) = ( 3.96e-04 ) ; ( R ) = ( 7.51e-03 ) ; + Last LinSolve(iter,res) = ( 2, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-04 ) ; ( Rwell ) = ( 4.54e-05 ) ; ( R ) = ( 1.71e-04 ) ; + Last LinSolve(iter,res) = ( 3, 3.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 4.89251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.171291 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.24938e+07, 1.25001e+07, 1.31116e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.734 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.94665e-05, 728.734 } rm^3 +compflowStatistics, reservoir: Phase mass: { 0.0113525, 703284 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 0.00331405, 210985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 0.00803841, 492299 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 0.0113525, 703284 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 0.0113525, 0 }, { 0.0174064, 703284 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.24954e+07, 1.25e+07, 1.25003e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.653 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.653 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214877 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64463.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150414 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214877 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22653e-08, 214877 } } kg +well_1Control: BHP (at the specified reference elevation): 23960094.51907003 Pa +well_1Control: Total rate: 0.00029566997749602594 kg/s; total surface volumetric rate: 2.0000000000000063e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987377e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855673e-17 sm3/s +compflowStatistics: Max phase CFL number: 1.57174 +compflowStatistics: Max component CFL number: 0.540281 +Time: 100s, dt:50.8989s, Cycle: 1 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 1.19e-03 ) ; ( R ) = ( 6.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 2.37e-03 ) ; ( R ) = ( 8.35e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-04 ) ; ( Rwell ) = ( 3.66e-05 ) ; ( R ) = ( 2.44e-04 ) ; + Last LinSolve(iter,res) = ( 2, 6.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23318529.329811733 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543888312e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0983323 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0741088 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 150.899s, dt:48.9822s, Cycle: 2 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 1.27e-03 ) ; ( R ) = ( 6.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 8.71e-04 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 2, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.62e-06 ) ; ( Rwell ) = ( 7.03e-06 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 3, 2.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.866458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0453794 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 199.881s, dt:63.9856s, Cycle: 3 +well_1Control: BHP (at the specified reference elevation): 22707592.635454517 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543887979e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 1.27e-03 ) ; ( R ) = ( 5.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 1.07e-03 ) ; ( R ) = ( 6.63e-03 ) ; + Last LinSolve(iter,res) = ( 3, 2.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.59e-06 ) ; ( Rwell ) = ( 4.61e-06 ) ; ( R ) = ( 9.75e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.486585 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0385064 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 263.867s, dt:91.4001s, Cycle: 4 +well_1Control: BHP (at the specified reference elevation): 22302837.349904392 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543872155e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 6.55e-04 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.25e-03 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-05 ) ; ( Rwell ) = ( 1.12e-05 ) ; ( R ) = ( 3.27e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 1.27412 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631086 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 355.267s, dt:97.8202s, Cycle: 5 +well_1Control: BHP (at the specified reference elevation): 22266867.026387226 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543856645e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 5.16e-05 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 6.65e-04 ) ; ( R ) = ( 6.02e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.41e-05 ) ; ( Rwell ) = ( 2.90e-06 ) ; ( R ) = ( 8.41e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.65889 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.060124 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 453.087s, dt:107.976s, Cycle: 6 +well_1Control: BHP (at the specified reference elevation): 22169078.200491354 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543858286e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.06e-04 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.91e-04 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.71e-05 ) ; ( Rwell ) = ( 9.55e-07 ) ; ( R ) = ( 4.71e-05 ) ; + Last LinSolve(iter,res) = ( 4, 1.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21978097.03180751 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543860298e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.408533 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0524852 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 561.063s, dt:129.593s, Cycle: 7 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.85e-04 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.07e-04 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 3, 3.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.80e-05 ) ; ( Rwell ) = ( 5.10e-07 ) ; ( R ) = ( 3.80e-05 ) ; + Last LinSolve(iter,res) = ( 3, 2.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.489011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0457201 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 690.657s, dt:168.574s, Cycle: 8 +well_1Control: BHP (at the specified reference elevation): 21783689.362432793 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543859577e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 1.58e-04 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.93e-04 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.58e-06 ) ; ( Rwell ) = ( 4.57e-07 ) ; ( R ) = ( 4.60e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-04 ) ; +well_1Control: BHP (at the specified reference elevation): 21613262.612977967 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543858289e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.431883 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0410159 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 859.231s, dt:232.85s, Cycle: 9 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.08e-04 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 3.02e-04 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-05 ) ; ( Rwell ) = ( 3.94e-07 ) ; ( R ) = ( 3.69e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.202758 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.039283 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1092.08s, dt:329.136s, Cycle: 10 +well_1Control: BHP (at the specified reference elevation): 21505652.577533297 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385685e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 4.96e-05 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 3.12e-04 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 5.18e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.08e-04 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.99e-05 ) ; ( Rwell ) = ( 4.16e-08 ) ; ( R ) = ( 3.99e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.576508 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0704917 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1421.22s, dt:327.602s, Cycle: 11 +well_1Control: BHP (at the specified reference elevation): 21536627.443183657 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.00e-05 ) ; ( R ) = ( 5.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.89e-04 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-04 ) ; ( Rwell ) = ( 2.36e-07 ) ; ( R ) = ( 1.90e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21505937.745190345 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855884e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.193627 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651505 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1748.82s, dt:343.465s, Cycle: 12 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 5.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 1.08e-04 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.37e-05 ) ; ( Rwell ) = ( 5.11e-08 ) ; ( R ) = ( 9.37e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.25e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21424186.79431143 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543856264e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.223699 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0494884 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2092.28s, dt:426.849s, Cycle: 13 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.55e-05 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.52e-03 ) ; ( Rwell ) = ( 9.41e-05 ) ; ( R ) = ( 8.52e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.07e-05 ) ; ( Rwell ) = ( 8.51e-08 ) ; ( R ) = ( 7.07e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.287094 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051387 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2519.13s, dt:518.819s, Cycle: 14 +well_1Control: BHP (at the specified reference elevation): 21329357.138129614 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543856224e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.39e-05 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 8.46e-05 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-05 ) ; ( Rwell ) = ( 3.28e-08 ) ; ( R ) = ( 1.56e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.48e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21271534.948864717 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855925e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.148031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0487288 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3037.95s, dt:650.624s, Cycle: 15 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.20e-05 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 9.18e-05 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-04 ) ; ( Rwell ) = ( 2.13e-08 ) ; ( R ) = ( 1.55e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.322158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066041 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3688.58s, dt:676.117s, Cycle: 16 +well_1Control: BHP (at the specified reference elevation): 21292545.637007818 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.49e-06 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 5.86e-05 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-04 ) ; ( Rwell ) = ( 3.59e-08 ) ; ( R ) = ( 1.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.171697 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644431 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4364.69s, dt:713.898s, Cycle: 17 +well_1Control: BHP (at the specified reference elevation): 21287078.78250073 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855657e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 9.05e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 3.78e-05 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.118959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0553678 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5078.59s, dt:829.491s, Cycle: 18 +well_1Control: BHP (at the specified reference elevation): 21245688.03946571 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855788e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 6.26e-06 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.02e-05 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-05 ) ; ( Rwell ) = ( 5.46e-09 ) ; ( R ) = ( 3.32e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.20261 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0500437 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5908.08s, dt:1024.14s, Cycle: 19 +well_1Control: BHP (at the specified reference elevation): 21185047.04677037 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855825e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 7.91e-06 ) ; ( R ) = ( 4.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.74e-05 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.86e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 8.40e-06 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-05 ) ; ( Rwell ) = ( 2.28e-08 ) ; ( R ) = ( 1.83e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.84e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21162765.622810952 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855691e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0863186 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0543462 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6932.22s, dt:1203.57s, Cycle: 20 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.33e-06 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 2.91e-05 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-04 ) ; ( Rwell ) = ( 2.42e-10 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.152757 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665449 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8135.79s, dt:1244.53s, Cycle: 21 +well_1Control: BHP (at the specified reference elevation): 21168347.645339176 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 5.01e-07 ) ; ( R ) = ( 5.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.94e-05 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 5.08e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 5.41e-06 ) ; ( R ) = ( 6.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-04 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 1.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.129842 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640702 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9380.32s, dt:1319.02s, Cycle: 22 +well_1Control: BHP (at the specified reference elevation): 21166945.916121125 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.24e-05 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.93e-04 ) ; ( Rwell ) = ( 7.67e-09 ) ; ( R ) = ( 1.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.131481 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568322 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 10699.3s, dt:1508.15s, Cycle: 23 +well_1Control: BHP (at the specified reference elevation): 21128458.88891556 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855713e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.15e-06 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.01e-05 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.37e-04 ) ; ( Rwell ) = ( 1.17e-07 ) ; ( R ) = ( 5.37e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0922853 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0499723 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 12207.5s, dt:1863.62s, Cycle: 24 +well_1Control: BHP (at the specified reference elevation): 21100125.667866834 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855686e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.92e-06 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 1.16e-05 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 1.94e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 3.42e-06 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.89e-05 ) ; ( Rwell ) = ( 8.80e-09 ) ; ( R ) = ( 6.89e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21102307.637977697 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.117001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685543 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 14071.1s, dt:1889.63s, Cycle: 25 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.36e-07 ) ; ( R ) = ( 5.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 8.65e-06 ) ; ( R ) = ( 4.62e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; ( R ) = ( 2.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21102962.694597647 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0886954 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633215 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 15960.7s, dt:2017.98s, Cycle: 26 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 5.71e-06 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-04 ) ; ( Rwell ) = ( 8.56e-10 ) ; ( R ) = ( 2.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0576331 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0615745 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 17978.7s, dt:2194.04s, Cycle: 27 +well_1Control: BHP (at the specified reference elevation): 21084965.961812582 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385566e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 9.67e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 4.67e-06 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.84e-05 ) ; ( Rwell ) = ( 3.29e-09 ) ; ( R ) = ( 9.84e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21066711.285551313 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385566e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0605389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566335 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 20172.8s, dt:2514.08s, Cycle: 28 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 9.00e-07 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 3.77e-06 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 4.90e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.04e-07 ) ; ( Rwell ) = ( 5.98e-13 ) ; ( R ) = ( 2.04e-07 ) ; + Last LinSolve(iter,res) = ( 9, 8.08e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0717093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650833 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 22686.8s, dt:2637.59s, Cycle: 29 +well_1Control: BHP (at the specified reference elevation): 21064690.3961963 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 8.73e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.47e-06 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 3, 4.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; ( R ) = ( 2.27e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0668571 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626932 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 25324.4s, dt:2834.87s, Cycle: 30 +well_1Control: BHP (at the specified reference elevation): 21065628.283446904 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.64e-06 ) ; ( R ) = ( 5.22e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.28e-10 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.85e-07 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 8.85e-07 ) ; + Last LinSolve(iter,res) = ( 6, 1.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0378048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0635717 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 28159.3s, dt:3019.74s, Cycle: 31 +well_1Control: BHP (at the specified reference elevation): 21057470.427231807 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855642e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.13e-07 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 1.97e-06 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 6.52e-11 ) ; ( R ) = ( 5.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0372038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059928 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 31179s, dt:3340.14s, Cycle: 32 +well_1Control: BHP (at the specified reference elevation): 21046193.685262766 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855642e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 4.06e-07 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 3, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 2.61e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.55e-05 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 8.55e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.065055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644419 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 34519.2s, dt:3526.83s, Cycle: 33 +well_1Control: BHP (at the specified reference elevation): 21046538.684589677 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.55e-06 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 3, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 3.92e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 4.20e-07 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.02e-05 ) ; ( Rwell ) = ( 2.46e-10 ) ; ( R ) = ( 7.02e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0580247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630289 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 38046s, dt:3777.63s, Cycle: 34 +well_1Control: BHP (at the specified reference elevation): 21048617.228614956 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 6.43e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-04 ) ; ( Rwell ) = ( 2.75e-10 ) ; ( R ) = ( 1.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0199638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0608767 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 41823.6s, dt:4137.1s, Cycle: 35 +well_1Control: BHP (at the specified reference elevation): 21042298.65209002 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855642e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.82e-07 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 8.12e-07 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.78e-04 ) ; ( Rwell ) = ( 1.38e-10 ) ; ( R ) = ( 2.78e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0317535 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.063761 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 45960.7s, dt:4398.45s, Cycle: 36 +well_1Control: BHP (at the specified reference elevation): 21038679.659343533 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855642e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 9.50e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 8.64e-07 ) ; ( R ) = ( 6.22e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 1.68e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 2.66e-07 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.67e-08 ) ; ( Rwell ) = ( 5.88e-15 ) ; ( R ) = ( 9.67e-08 ) ; + Last LinSolve(iter,res) = ( 8, 5.14e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0596779 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659348 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 50359.2s, dt:4575.6s, Cycle: 37 +well_1Control: BHP (at the specified reference elevation): 21041659.50411418 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 7.37e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 6.49e-07 ) ; ( R ) = ( 6.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.99e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.06e-07 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-04 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 1.99e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0446452 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630971 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 54934.8s, dt:4897.58s, Cycle: 38 +well_1Control: BHP (at the specified reference elevation): 21042987.895646635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.72e-07 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-07 ) ; ( Rwell ) = ( 9.72e-14 ) ; ( R ) = ( 3.92e-07 ) ; + Last LinSolve(iter,res) = ( 7, 9.61e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0291749 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607956 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 59832.4s, dt:5368.16s, Cycle: 39 +well_1Control: BHP (at the specified reference elevation): 21039312.720203176 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 8.16e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 5.34e-07 ) ; ( R ) = ( 6.92e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 9.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.45e-07 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-04 ) ; ( Rwell ) = ( 3.04e-10 ) ; ( R ) = ( 1.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0511402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682106 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 65200.5s, dt:5461.22s, Cycle: 40 +well_1Control: BHP (at the specified reference elevation): 21042206.371694762 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 4.14e-07 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 1.13e-07 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 2.99e-10 ) ; ( R ) = ( 3.95e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0503219 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064534 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 70661.8s, dt:5761.13s, Cycle: 41 +well_1Control: BHP (at the specified reference elevation): 21045340.52919019 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.50e-07 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.07e-04 ) ; ( Rwell ) = ( 3.49e-10 ) ; ( R ) = ( 5.07e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0467693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630871 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 76422.9s, dt:6167.16s, Cycle: 42 +well_1Control: BHP (at the specified reference elevation): 21048204.475743975 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 4.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-06 ) ; ( Rwell ) = ( 9.75e-14 ) ; ( R ) = ( 2.11e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0370002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061381 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 82590s, dt:6718.67s, Cycle: 43 +well_1Control: BHP (at the specified reference elevation): 21049617.801980153 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 2.89e-07 ) ; ( R ) = ( 6.25e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 7.77e-08 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 6.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.35e-05 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 7.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0470118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683886 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 89308.7s, dt:6823.38s, Cycle: 44 +well_1Control: BHP (at the specified reference elevation): 21053161.572769232 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 5.73e-08 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 3.24e-07 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 1.21e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 6.58e-08 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 7.83e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0575419 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655107 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 96132.1s, dt:7128.15s, Cycle: 45 +well_1Control: BHP (at the specified reference elevation): 21059177.77428484 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 9.59e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.67e-07 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 8.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 6.30e-08 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-04 ) ; ( Rwell ) = ( 4.77e-11 ) ; ( R ) = ( 3.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0433861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0634608 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 103260s, dt:7601.56s, Cycle: 46 +well_1Control: BHP (at the specified reference elevation): 21063416.307039842 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 6.46e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 6.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 5.40e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.77e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; ( R ) = ( 6.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.42e-06 ) ; ( Rwell ) = ( 1.64e-12 ) ; ( R ) = ( 8.42e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0440422 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677095 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 110862s, dt:7771.08s, Cycle: 47 +well_1Control: BHP (at the specified reference elevation): 21067271.105211325 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 5.77e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 6.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 5.12e-08 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.64e-04 ) ; ( Rwell ) = ( 1.29e-10 ) ; ( R ) = ( 2.64e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0600218 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657419 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 118633s, dt:8099.55s, Cycle: 48 +well_1Control: BHP (at the specified reference elevation): 21075544.97367105 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 1.43e-07 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 9.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-04 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 2.01e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0458012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639975 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 126732s, dt:8590.64s, Cycle: 49 +well_1Control: BHP (at the specified reference elevation): 21080762.20622588 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 6.99e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 4.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-04 ) ; ( Rwell ) = ( 1.05e-13 ) ; ( R ) = ( 1.78e-04 ) ; + Last LinSolve(iter,res) = ( 7, 1.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0402702 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621299 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 135323s, dt:9286.72s, Cycle: 50 +well_1Control: BHP (at the specified reference elevation): 21085380.188873354 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 6.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-04 ) ; ( Rwell ) = ( 1.64e-10 ) ; ( R ) = ( 3.92e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.38e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21095992.532775737 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0675707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692894 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 144610s, dt:9349.99s, Cycle: 51 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.24e-07 ) ; ( R ) = ( 5.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 9.91e-08 ) ; ( R ) = ( 6.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 8.68e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-04 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0478857 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659325 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 153960s, dt:9726.79s, Cycle: 52 +well_1Control: BHP (at the specified reference elevation): 21102680.55057802 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 7.76e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 7.02e-08 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.75e-04 ) ; ( Rwell ) = ( 9.69e-11 ) ; ( R ) = ( 3.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0547666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644992 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 163687s, dt:10264.5s, Cycle: 53 +well_1Control: BHP (at the specified reference elevation): 21111027.768331833 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 9.31e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 6.56e-08 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 6.30e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-04 ) ; ( Rwell ) = ( 8.72e-11 ) ; ( R ) = ( 3.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0547333 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676493 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 173951s, dt:10499.6s, Cycle: 54 +well_1Control: BHP (at the specified reference elevation): 21118969.02264758 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 8.39e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 5.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.95e-05 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 4.95e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0617095 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662328 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 184451s, dt:10890.3s, Cycle: 55 +well_1Control: BHP (at the specified reference elevation): 21129485.568196863 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 8.85e-08 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 7.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.63e-04 ) ; ( Rwell ) = ( 5.57e-11 ) ; ( R ) = ( 3.63e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0607774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648919 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 195341s, dt:11447.2s, Cycle: 56 +well_1Control: BHP (at the specified reference elevation): 21139772.588740014 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 8.96e-08 ) ; ( R ) = ( 5.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.87e-06 ) ; ( Rwell ) = ( 1.12e-14 ) ; ( R ) = ( 7.87e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0529579 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642881 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 206788s, dt:12105.8s, Cycle: 57 +well_1Control: BHP (at the specified reference elevation): 21147957.201672148 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 7.74e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 6.70e-08 ) ; ( R ) = ( 6.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 5.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 2.81e-10 ) ; ( R ) = ( 5.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.068222 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688524 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 218894s, dt:12239.5s, Cycle: 58 +well_1Control: BHP (at the specified reference elevation): 21160074.900611907 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.09e-07 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 6.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 7.53e-11 ) ; ( R ) = ( 5.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0661996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651979 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 231134s, dt:12826.1s, Cycle: 59 +well_1Control: BHP (at the specified reference elevation): 21171945.105134882 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 6.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 1.41e-10 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0570015 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652777 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 243960s, dt:13430.1s, Cycle: 60 +well_1Control: BHP (at the specified reference elevation): 21182114.15902918 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 8.57e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 5.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.25e-10 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0728522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685164 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 257390s, dt:13622.6s, Cycle: 61 +well_1Control: BHP (at the specified reference elevation): 21195552.403751332 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; ( R ) = ( 6.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 6.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 1.90e-10 ) ; ( R ) = ( 8.87e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0672987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666162 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 271012s, dt:14076.2s, Cycle: 62 +well_1Control: BHP (at the specified reference elevation): 21208207.52913052 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.79e-04 ) ; ( Rwell ) = ( 7.41e-11 ) ; ( R ) = ( 4.79e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0696961 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654194 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 285089s, dt:14718.3s, Cycle: 63 +well_1Control: BHP (at the specified reference elevation): 21221764.674449354 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 6.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 6.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-05 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 1.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21233798.28597523 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0645741 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637888 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 299807s, dt:15643.7s, Cycle: 64 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 8.81e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 2.38e-07 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 8.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; ( R ) = ( 2.90e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 1.12e-10 ) ; ( R ) = ( 4.86e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0805231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689387 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 315451s, dt:15803.5s, Cycle: 65 +well_1Control: BHP (at the specified reference elevation): 21249944.756268807 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 6.91e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 5.63e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0716012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670414 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 331254s, dt:16261.7s, Cycle: 66 +well_1Control: BHP (at the specified reference elevation): 21264456.51583918 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 9.88e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 6.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 8.76e-11 ) ; ( R ) = ( 4.85e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21278801.568425756 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0741701 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654988 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 347516s, dt:16990s, Cycle: 67 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 9.49e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 5.02e-08 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 6.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-04 ) ; ( Rwell ) = ( 2.41e-10 ) ; ( R ) = ( 3.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0818339 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681914 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 364506s, dt:17287.8s, Cycle: 68 +well_1Control: BHP (at the specified reference elevation): 21295725.33967483 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; ( R ) = ( 6.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 8.81e-11 ) ; ( R ) = ( 4.80e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0786096 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659535 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 381794s, dt:17980.7s, Cycle: 69 +well_1Control: BHP (at the specified reference elevation): 21311825.61930333 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 6.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 1.45e-10 ) ; ( R ) = ( 7.54e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.97e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21328465.662068833 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0791068 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 399774s, dt:18593.9s, Cycle: 70 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 9.94e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 2.82e-07 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 8.98e-11 ) ; ( R ) = ( 6.76e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0847374 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682837 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 418368s, dt:18902.8s, Cycle: 71 +well_1Control: BHP (at the specified reference elevation): 21346103.585277483 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; ( R ) = ( 6.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 6.29e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-04 ) ; ( Rwell ) = ( 1.22e-10 ) ; ( R ) = ( 4.17e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0833516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668593 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 437271s, dt:19485.7s, Cycle: 72 +well_1Control: BHP (at the specified reference elevation): 21363738.833304286 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 6.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 8.54e-11 ) ; ( R ) = ( 7.38e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0865244 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664209 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 456757s, dt:20173.3s, Cycle: 73 +well_1Control: BHP (at the specified reference elevation): 21382351.3980066 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; ( R ) = ( 6.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 6.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; ( R ) = ( 2.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.14e-10 ) ; ( R ) = ( 8.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0866883 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661312 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 476930s, dt:20945.1s, Cycle: 74 +well_1Control: BHP (at the specified reference elevation): 21400960.446924884 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 9.89e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 5.58e-08 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 6.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 9.36e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0918597 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678696 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 497875s, dt:21378.9s, Cycle: 75 +well_1Control: BHP (at the specified reference elevation): 21420712.166066587 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.48e-07 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 6.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.80e-07 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 1.86e-10 ) ; ( R ) = ( 7.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21440945.67324298 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0918656 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672513 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 519254s, dt:21953.5s, Cycle: 76 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 6.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 4.11e-09 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.15e-04 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 1.15e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0917148 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662618 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 541208s, dt:22764s, Cycle: 77 +well_1Control: BHP (at the specified reference elevation): 21461168.537248887 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 9.82e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 4.87e-08 ) ; ( R ) = ( 6.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.89e-10 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.06e-06 ) ; ( Rwell ) = ( 4.06e-14 ) ; ( R ) = ( 4.06e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0976314 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682693 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 563972s, dt:23145.5s, Cycle: 78 +well_1Control: BHP (at the specified reference elevation): 21482719.989179082 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 5.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 6.51e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.00e-04 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.00e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21505213.91728454 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0997669 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067155 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 587117s, dt:23790.1s, Cycle: 79 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 6.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 7.37e-10 ) ; ( R ) = ( 6.52e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.094807 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661872 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 610907s, dt:24686.5s, Cycle: 80 +well_1Control: BHP (at the specified reference elevation): 21525898.705832563 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 9.32e-08 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 5.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.62e-10 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.70e-06 ) ; ( Rwell ) = ( 3.74e-14 ) ; ( R ) = ( 3.70e-06 ) ; + Last LinSolve(iter,res) = ( 9, 9.58e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.104655 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681502 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 635594s, dt:25129.2s, Cycle: 81 +well_1Control: BHP (at the specified reference elevation): 21549368.468645975 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 6.21e-08 ) ; ( R ) = ( 6.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 6.60e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 4.45e-11 ) ; ( R ) = ( 6.03e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.105701 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674742 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 660723s, dt:25748.6s, Cycle: 82 +well_1Control: BHP (at the specified reference elevation): 21573379.67447199 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 5.61e-08 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 6.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.07e-04 ) ; ( Rwell ) = ( 4.22e-11 ) ; ( R ) = ( 5.07e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.105262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667188 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 686471s, dt:26579.2s, Cycle: 83 +well_1Control: BHP (at the specified reference elevation): 21597307.662529927 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 9.85e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 5.52e-08 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 6.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 9.18e-11 ) ; ( R ) = ( 7.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.108029 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678997 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 713051s, dt:27121.7s, Cycle: 84 +well_1Control: BHP (at the specified reference elevation): 21621901.80827649 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.80e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 6.20e-07 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 3.42e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 7.29e-11 ) ; ( R ) = ( 8.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.108991 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668365 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 740172s, dt:27964.2s, Cycle: 85 +well_1Control: BHP (at the specified reference elevation): 21646891.816079967 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.75e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 6.06e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.45e-10 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.63e-06 ) ; ( Rwell ) = ( 1.89e-14 ) ; ( R ) = ( 4.63e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.111926 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670737 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 768136s, dt:28765.9s, Cycle: 86 +well_1Control: BHP (at the specified reference elevation): 21672908.988172963 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.82e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 7.22e-08 ) ; ( R ) = ( 5.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 6.72e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 5.67e-11 ) ; ( R ) = ( 7.78e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.113746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662802 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 796902s, dt:29822.4s, Cycle: 87 +well_1Control: BHP (at the specified reference elevation): 21699379.461625583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.71e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 6.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 6.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.24e-07 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 9.89e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.119654 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694737 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 826725s, dt:29972.6s, Cycle: 88 +well_1Control: BHP (at the specified reference elevation): 21727146.504378617 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 9.81e-08 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; ( R ) = ( 5.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 6.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 5.57e-11 ) ; ( R ) = ( 8.16e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670414 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 856697s, dt:30841.7s, Cycle: 89 +well_1Control: BHP (at the specified reference elevation): 21754617.51988659 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 9.64e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 6.88e-08 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 6.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.49e-06 ) ; ( Rwell ) = ( 2.70e-14 ) ; ( R ) = ( 5.49e-06 ) ; + Last LinSolve(iter,res) = ( 9, 1.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.120268 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662586 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 887539s, dt:31981.2s, Cycle: 90 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 21782562.065620027 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 9.51e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 7.57e-08 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 6.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 5.73e-11 ) ; ( R ) = ( 4.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.126408 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686289 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 919520s, dt:32404.4s, Cycle: 91 +well_1Control: BHP (at the specified reference elevation): 21812356.52582708 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.78e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 6.70e-07 ) ; ( R ) = ( 5.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 3.36e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 7.60e-11 ) ; ( R ) = ( 7.38e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.127618 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670203 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 951925s, dt:33350.8s, Cycle: 92 +well_1Control: BHP (at the specified reference elevation): 21842596.957502812 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 9.78e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 7.90e-08 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 6.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 7.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.03e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21872345.713594973 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.129338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673961 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 985275s, dt:14724.6s, Cycle: 93 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 9.33e-08 ) ; ( R ) = ( 2.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 7.08e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.83e-03 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.33e-03 ) ; ( Rwell ) = ( 8.19e-10 ) ; ( R ) = ( 6.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.16e-05 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 4.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0606888 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0297021 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1e+06s, dt:23895.5s, Cycle: 94 +well_1Control: BHP (at the specified reference elevation): 21886320.838349022 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 9.92e-08 ) ; ( R ) = ( 3.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 4.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-03 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 8.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0923636 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0490746 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.3009e+07, 1.30513e+07, 1.31983e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 497290, 687048 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.135 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.798408, 728.337 } rm^3 +compflowStatistics, reservoir: Phase mass: { 229.575, 703215 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 35.2501, 211198 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 194.325, 492017 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.575351, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 229, 703215 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 229.575, 0 }, { 73.1679, 703140 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.26312e+07, 1.28791e+07, 1.30276e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 123679, 515888 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.737 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.737 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215021 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64506.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150515 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215021 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22804e-08, 215021 } } kg +well_1Control: BHP (at the specified reference elevation): 21907994.684887663 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 5.03772 +compflowStatistics: Max component CFL number: 142.771 +Time: 1.0239e+06s, dt:29842.8s, Cycle: 95 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 9.47e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 5.77e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 2.81e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-04 ) ; ( Rwell ) = ( 4.37e-11 ) ; ( R ) = ( 3.47e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21935733.306441076 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.115723 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598969 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.05374e+06s, dt:33020s, Cycle: 96 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 9.70e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 7.27e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 6.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 4.69e-11 ) ; ( R ) = ( 5.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.127049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636756 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08676e+06s, dt:35136.4s, Cycle: 97 +well_1Control: BHP (at the specified reference elevation): 21965643.64827846 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 9.44e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 6.72e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 1.08e-10 ) ; ( R ) = ( 7.70e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.134727 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662234 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.12189e+06s, dt:36447.3s, Cycle: 98 +well_1Control: BHP (at the specified reference elevation): 21996963.819050044 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 9.28e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 5.28e-07 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.09e-10 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 4.04e-14 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.139195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678203 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15834e+06s, dt:37219.9s, Cycle: 99 +well_1Control: BHP (at the specified reference elevation): 22030142.86323715 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 9.45e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 8.99e-08 ) ; ( R ) = ( 5.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 6.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 4.03e-11 ) ; ( R ) = ( 6.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.141515 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662314 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.19556e+06s, dt:38605.6s, Cycle: 100 +well_1Control: BHP (at the specified reference elevation): 22063510.217857227 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 9.30e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 9.02e-08 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 6.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.09e-10 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.60e-06 ) ; ( Rwell ) = ( 1.67e-14 ) ; ( R ) = ( 2.60e-06 ) ; + Last LinSolve(iter,res) = ( 10, 1.59e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22098184.963097855 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.146085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661319 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.23417e+06s, dt:40082.2s, Cycle: 101 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.30e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 7.05e-07 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 3.01e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.70e-11 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-06 ) ; ( Rwell ) = ( 1.12e-15 ) ; ( R ) = ( 1.40e-06 ) ; + Last LinSolve(iter,res) = ( 10, 1.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.150918 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0700513 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.27425e+06s, dt:40062.6s, Cycle: 102 +well_1Control: BHP (at the specified reference elevation): 22134242.774249807 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 9.30e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 9.02e-08 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 6.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.80e-11 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-06 ) ; ( Rwell ) = ( 1.35e-15 ) ; ( R ) = ( 1.25e-06 ) ; + Last LinSolve(iter,res) = ( 10, 1.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.150108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674305 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31431e+06s, dt:41067.6s, Cycle: 103 +well_1Control: BHP (at the specified reference elevation): 22170283.292576082 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.28e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 7.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.97e-11 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.03e-06 ) ; ( Rwell ) = ( 7.98e-15 ) ; ( R ) = ( 3.03e-06 ) ; + Last LinSolve(iter,res) = ( 10, 1.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.153095 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663997 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35538e+06s, dt:42525.7s, Cycle: 104 +well_1Control: BHP (at the specified reference elevation): 22206704.054555982 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 9.14e-08 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 7.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 4.46e-11 ) ; ( R ) = ( 8.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.157716 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694672 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39791e+06s, dt:42742.6s, Cycle: 105 +well_1Control: BHP (at the specified reference elevation): 22244818.388185896 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 9.22e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 7.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 7.70e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.157708 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067662 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.44065e+06s, dt:43716s, Cycle: 106 +well_1Control: BHP (at the specified reference elevation): 22282820.879903473 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 9.13e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.96e-11 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.81e-06 ) ; ( Rwell ) = ( 8.31e-15 ) ; ( R ) = ( 1.81e-06 ) ; + Last LinSolve(iter,res) = ( 10, 1.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22321560.31664194 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.160445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06676 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48436e+06s, dt:45107.9s, Cycle: 107 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 9.08e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 7.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 9.76e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.17e-05 ) ; ( Rwell ) = ( 3.18e-14 ) ; ( R ) = ( 3.17e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.164608 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696966 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52947e+06s, dt:45238.6s, Cycle: 108 +well_1Control: BHP (at the specified reference elevation): 22361133.164749376 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 8.97e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.76e-07 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 7.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.39e-07 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 7.43e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.164203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676805 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57471e+06s, dt:46260.6s, Cycle: 109 +well_1Control: BHP (at the specified reference elevation): 22401514.92903352 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.11e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 7.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.167011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664389 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.62097e+06s, dt:47884.6s, Cycle: 110 +well_1Control: BHP (at the specified reference elevation): 22442100.894606896 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 8.94e-08 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 7.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.59e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 2.75e-14 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 9, 3.67e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22483777.618212204 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.171855 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687836 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.66886e+06s, dt:48445.8s, Cycle: 111 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 8.85e-08 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 7.37e-07 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.90e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.18e-11 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.50e-06 ) ; ( Rwell ) = ( 6.48e-15 ) ; ( R ) = ( 2.50e-06 ) ; + Last LinSolve(iter,res) = ( 10, 2.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.172857 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671711 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.7173e+06s, dt:49787.2s, Cycle: 112 +well_1Control: BHP (at the specified reference elevation): 22526406.798077412 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 8.93e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 5.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 7.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 3.94e-11 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.176677 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06768 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.76709e+06s, dt:50912.1s, Cycle: 113 +well_1Control: BHP (at the specified reference elevation): 22570120.751928594 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 8.89e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 5.51e-07 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 8.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 8.46e-11 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.93e-06 ) ; ( Rwell ) = ( 2.37e-14 ) ; ( R ) = ( 7.93e-06 ) ; + Last LinSolve(iter,res) = ( 10, 2.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.17958 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668065 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.818e+06s, dt:52509.1s, Cycle: 114 +well_1Control: BHP (at the specified reference elevation): 22613918.94473175 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 8.69e-08 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 7.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 4.57e-11 ) ; ( R ) = ( 7.17e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.184355 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701513 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.87051e+06s, dt:52433.6s, Cycle: 115 +well_1Control: BHP (at the specified reference elevation): 22659403.929947644 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 8.74e-08 ) ; ( R ) = ( 5.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 4.04e-07 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 7.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 3.51e-07 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 3.90e-11 ) ; ( R ) = ( 7.60e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.183305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672781 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.92294e+06s, dt:53829s, Cycle: 116 +well_1Control: BHP (at the specified reference elevation): 22704728.85313239 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 8.70e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.28e-07 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 7.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 5.56e-11 ) ; ( R ) = ( 6.00e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.187423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668476 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.97677e+06s, dt:23227.3s, Cycle: 117 +well_1Control: BHP (at the specified reference elevation): 22751127.041908544 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 8.66e-08 ) ; ( R ) = ( 2.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-04 ) ; ( Rwell ) = ( 3.06e-10 ) ; ( R ) = ( 1.65e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0821642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0299016 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2e+06s, dt:37577.9s, Cycle: 118 +well_1Control: BHP (at the specified reference elevation): 22771932.11849842 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 9.02e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 3.93e-07 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 5.60e-11 ) ; ( R ) = ( 7.91e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.130223 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0483547 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.34819e+07, 1.3524e+07, 1.36597e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 964848, 1.14315e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.479 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.53851, 727.94 } rm^3 +compflowStatistics, reservoir: Phase mass: { 465.618, 703101 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 70.4442, 211380 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 395.174, 491721 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.907731, 0.0675228 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 464.71, 703101 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 465.618, 0 }, { 136.842, 702961 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.30322e+07, 1.33496e+07, 1.35003e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 515814, 983323 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.842 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.842 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215200 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64559.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150640 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215200 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22989e-08, 215200 } } kg +well_1Control: BHP (at the specified reference elevation): 22804306.967161816 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 8.22074 +compflowStatistics: Max component CFL number: 213.568 +Time: 2.03758e+06s, dt:47336s, Cycle: 119 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 8.64e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 9.76e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 6.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 8.87e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.163613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594414 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.08491e+06s, dt:52628.1s, Cycle: 120 +well_1Control: BHP (at the specified reference elevation): 22844868.479247957 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 8.57e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 7.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.40e-07 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 7.82e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.181344 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636552 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.13754e+06s, dt:56012.8s, Cycle: 121 +well_1Control: BHP (at the specified reference elevation): 22889287.659330733 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 8.42e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.27e-07 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 7.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 3.61e-11 ) ; ( R ) = ( 7.42e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.19234 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686884 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.19355e+06s, dt:56721.3s, Cycle: 122 +well_1Control: BHP (at the specified reference elevation): 22936576.348133303 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 8.41e-08 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 7.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 7.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.37e-07 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 9.68e-08 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-04 ) ; ( Rwell ) = ( 8.77e-12 ) ; ( R ) = ( 1.58e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.194073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666689 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.25028e+06s, dt:58579.7s, Cycle: 123 +well_1Control: BHP (at the specified reference elevation): 22984963.360591974 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 4.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 7.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 6.64e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.199704 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661435 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.30886e+06s, dt:60813.3s, Cycle: 124 +well_1Control: BHP (at the specified reference elevation): 23034400.876632005 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 8.37e-08 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 2.23e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 7.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.59e-07 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.54e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.206551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690096 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.36967e+06s, dt:61392.4s, Cycle: 125 +well_1Control: BHP (at the specified reference elevation): 23085502.5738056 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 8.31e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.42e-07 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 7.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 4.27e-11 ) ; ( R ) = ( 5.35e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.78e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23136820.97007133 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.207734 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677815 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.43106e+06s, dt:62717.6s, Cycle: 126 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 8.25e-08 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 3.21e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 7.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.54e-07 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 5.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.37e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23189116.840167586 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.211409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672454 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.49378e+06s, dt:64407.3s, Cycle: 127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 8.21e-08 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.47e-07 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 7.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.04e-11 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.65e-06 ) ; ( Rwell ) = ( 6.66e-15 ) ; ( R ) = ( 4.65e-06 ) ; + Last LinSolve(iter,res) = ( 11, 2.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.216259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681467 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.55819e+06s, dt:65564.5s, Cycle: 128 +well_1Control: BHP (at the specified reference elevation): 23242773.85948616 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 8.17e-08 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 4.95e-07 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 7.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 4.16e-07 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 5.94e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.219264 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069199 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.62375e+06s, dt:66068.5s, Cycle: 129 +well_1Control: BHP (at the specified reference elevation): 23297095.31645397 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 8.11e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 7.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 5.64e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.220049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674809 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.68982e+06s, dt:67692.6s, Cycle: 130 +well_1Control: BHP (at the specified reference elevation): 23351854.206868306 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 8.09e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 6.87e-07 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.87e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 7.86e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.224521 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666388 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.75751e+06s, dt:69931.2s, Cycle: 131 +well_1Control: BHP (at the specified reference elevation): 23407321.072547287 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 7.98e-08 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.57e-07 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 7.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.35e-11 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.42e-06 ) ; ( Rwell ) = ( 1.07e-14 ) ; ( R ) = ( 8.42e-06 ) ; + Last LinSolve(iter,res) = ( 12, 1.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.230931 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0702239 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.82744e+06s, dt:69782.4s, Cycle: 132 +well_1Control: BHP (at the specified reference elevation): 23464581.950046957 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 7.95e-08 ) ; ( R ) = ( 4.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 9.21e-07 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 4.21e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 9.02e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.229411 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675041 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.89723e+06s, dt:71481.5s, Cycle: 133 +well_1Control: BHP (at the specified reference elevation): 23521691.610985234 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 7.93e-08 ) ; ( R ) = ( 4.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.01e-07 ) ; ( R ) = ( 5.34e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 7.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 2.19e-07 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 7.31e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.233922 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670479 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.96871e+06s, dt:31293s, Cycle: 134 +well_1Control: BHP (at the specified reference elevation): 23579914.202058226 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 7.87e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 6.88e-11 ) ; ( R ) = ( 4.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.102063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0301001 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3e+06s, dt:50472.5s, Cycle: 135 +well_1Control: BHP (at the specified reference elevation): 23606041.84665551 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 8.06e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 7.87e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 6.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 5.40e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.164164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0485937 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.39191e+07, 1.3961e+07, 1.40902e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.39786e+06, 1.56939e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.796 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.22451, 727.572 } rm^3 +compflowStatistics, reservoir: Phase mass: { 705.027, 702994 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 105.864, 211549 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 599.163, 491445 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.16057, 0.0675355 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 703.867, 702994 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 705.027, 0 }, { 196.915, 702793 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.34786e+07, 1.37934e+07, 1.39375e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 956552, 1.41633e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.94 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.94 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215368 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64610.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150758 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215368 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23164e-08, 215368 } } kg +well_1Control: BHP (at the specified reference elevation): 23646925.629836824 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 10.4846 +compflowStatistics: Max component CFL number: 274.282 +Time: 3.05047e+06s, dt:63397.2s, Cycle: 136 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 7.80e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 5.50e-07 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.45e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-04 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.35e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.205396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593424 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.11387e+06s, dt:70559s, Cycle: 137 +well_1Control: BHP (at the specified reference elevation): 23697957.83570385 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 7.74e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.43e-07 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 7.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 6.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.227504 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643989 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.18443e+06s, dt:74535s, Cycle: 138 +well_1Control: BHP (at the specified reference elevation): 23754464.46448581 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 7.67e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 8.24e-07 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 3.42e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.41e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.02e-06 ) ; ( Rwell ) = ( 3.60e-15 ) ; ( R ) = ( 7.02e-06 ) ; + Last LinSolve(iter,res) = ( 11, 1.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.239023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669399 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.25896e+06s, dt:76772.5s, Cycle: 139 +well_1Control: BHP (at the specified reference elevation): 23814234.506560896 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 7.66e-08 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 3.03e-07 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 7.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.09e-07 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 9.92e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.244748 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669923 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.33574e+06s, dt:79036.4s, Cycle: 140 +well_1Control: BHP (at the specified reference elevation): 23875102.761495102 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 7.56e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 1.68e-07 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 7.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 4.91e-08 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 5.87e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.250386 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678545 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.41477e+06s, dt:80685.1s, Cycle: 141 +well_1Control: BHP (at the specified reference elevation): 23937824.87518942 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 7.54e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 6.76e-07 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 5.10e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24001468.374130964 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.253926 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683746 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.49546e+06s, dt:81953.7s, Cycle: 142 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 7.47e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.23e-07 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 8.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 8.78e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.256161 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684074 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.57741e+06s, dt:83215.9s, Cycle: 143 +well_1Control: BHP (at the specified reference elevation): 24065910.044337302 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 7.43e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 1.76e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 8.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 5.08e-08 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.33e-05 ) ; ( Rwell ) = ( 8.20e-15 ) ; ( R ) = ( 6.33e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.258294 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068295 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.66063e+06s, dt:84589.5s, Cycle: 144 +well_1Control: BHP (at the specified reference elevation): 24131230.967852138 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 7.39e-08 ) ; ( R ) = ( 4.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 6.35e-07 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 1.48e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 6.57e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.93e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24197220.170052946 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690705 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.74522e+06s, dt:85345s, Cycle: 145 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 7.32e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.36e-07 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 8.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 8.70e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.13e-05 ) ; ( Rwell ) = ( 1.09e-14 ) ; ( R ) = ( 5.13e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.261124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675555 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.83056e+06s, dt:87379.3s, Cycle: 146 +well_1Control: BHP (at the specified reference elevation): 24263555.782854017 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 7.27e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 1.77e-07 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 8.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 5.07e-08 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.265366 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675264 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.91794e+06s, dt:82058.9s, Cycle: 147 +well_1Control: BHP (at the specified reference elevation): 24330784.66626302 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 7.18e-08 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 5.78e-07 ) ; ( R ) = ( 4.83e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.50e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.16e-04 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.16e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.247414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633925 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4e+06s, dt:87569.5s, Cycle: 148 +well_1Control: BHP (at the specified reference elevation): 24394159.662381865 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 7.18e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 2.38e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 7.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 9.49e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.262091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668711 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 24461291.854806624 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.43377e+07, 1.43794e+07, 1.45041e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.80329e+06, 1.97002e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.101 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.87999, 727.221 } rm^3 +compflowStatistics, reservoir: Phase mass: { 952.764, 702892 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 142.629, 211710 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 810.135, 491182 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.49956, 0.0675647 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 951.264, 702892 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 952.764, 0 }, { 255.816, 702631 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.39208e+07, 1.42193e+07, 1.43562e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.38446e+06, 1.82176e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.035 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.035 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215530 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64659 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150871 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215530 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23331e-08, 215530 } } kg +compflowStatistics: Max phase CFL number: 17.0681 +compflowStatistics: Max component CFL number: 456.489 +Time: 4.08757e+06s, dt:90259.2s, Cycle: 149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 7.11e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.75e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 7.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.22e-06 ) ; ( Rwell ) = ( 5.48e-15 ) ; ( R ) = ( 8.22e-06 ) ; + Last LinSolve(iter,res) = ( 11, 2.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.268068 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659955 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.17783e+06s, dt:93837.9s, Cycle: 150 +well_1Control: BHP (at the specified reference elevation): 24529976.510196052 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 7.03e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 6.77e-07 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.13e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 6.34e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.276479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674426 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.27167e+06s, dt:96180.6s, Cycle: 151 +well_1Control: BHP (at the specified reference elevation): 24601259.650005583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 7.00e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 4.06e-07 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 8.30e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.82e-07 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.76e-05 ) ; ( Rwell ) = ( 5.88e-15 ) ; ( R ) = ( 3.76e-05 ) ; + Last LinSolve(iter,res) = ( 10, 5.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24673759.60641773 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688969 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.36785e+06s, dt:97201.7s, Cycle: 152 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 6.92e-08 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.87e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 8.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 5.86e-15 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 11, 4.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.281686 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671408 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.46505e+06s, dt:99922.7s, Cycle: 153 +well_1Control: BHP (at the specified reference elevation): 24746986.331097297 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 6.89e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 8.70e-07 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 4.11e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 5.36e-08 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.13e-05 ) ; ( Rwell ) = ( 2.81e-14 ) ; ( R ) = ( 5.13e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.28712 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679733 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.56497e+06s, dt:101889s, Cycle: 154 +well_1Control: BHP (at the specified reference elevation): 24821488.00834225 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 6.79e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 6.30e-07 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.79e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 5.53e-08 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.94e-05 ) ; ( Rwell ) = ( 1.49e-14 ) ; ( R ) = ( 5.94e-05 ) ; + Last LinSolve(iter,res) = ( 10, 8.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.290253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679353 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.66686e+06s, dt:103933s, Cycle: 155 +well_1Control: BHP (at the specified reference elevation): 24897421.896697246 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 6.77e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 4.22e-07 ) ; ( R ) = ( 5.36e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 8.32e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.95e-07 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.54e-05 ) ; ( Rwell ) = ( 1.14e-14 ) ; ( R ) = ( 6.54e-05 ) ; + Last LinSolve(iter,res) = ( 10, 9.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.293491 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684624 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.77079e+06s, dt:105478s, Cycle: 156 +well_1Control: BHP (at the specified reference elevation): 24974285.351026945 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 6.69e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.32e-07 ) ; ( R ) = ( 5.33e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 8.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.82e-06 ) ; ( Rwell ) = ( 2.28e-15 ) ; ( R ) = ( 9.82e-06 ) ; + Last LinSolve(iter,res) = ( 12, 2.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.295222 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067964 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.87627e+06s, dt:107563s, Cycle: 157 +well_1Control: BHP (at the specified reference elevation): 25051872.934678055 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 6.63e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.99e-07 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 8.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 5.56e-08 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 11, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.58e-05 ) ; ( Rwell ) = ( 3.49e-15 ) ; ( R ) = ( 4.58e-05 ) ; + Last LinSolve(iter,res) = ( 11, 6.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.29837 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688497 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.98384e+06s, dt:16164.8s, Cycle: 158 +well_1Control: BHP (at the specified reference elevation): 25130673.669039 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.05e-03 ) ; ( Rwell ) = ( 6.58e-08 ) ; ( R ) = ( 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-05 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 2.55e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0446652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0104205 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5e+06s, dt:32329.6s, Cycle: 159 +well_1Control: BHP (at the specified reference elevation): 25143077.297023557 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.89e-08 ) ; ( R ) = ( 1.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.00e-07 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-04 ) ; ( Rwell ) = ( 5.08e-11 ) ; ( R ) = ( 3.32e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.089133 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0206382 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 25167261.00310333 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.46985e+07, 1.47401e+07, 1.48618e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.18614e+06, 2.34952e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.363 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.44378, 726.919 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1180.85, 702805 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 176.284, 211850 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1004.57, 490956 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.84066, 0.0675949 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1179.01, 702805 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1180.85, 0 }, { 307.063, 702492 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.43021e+07, 1.45856e+07, 1.4717e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.78935e+06, 2.20463e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.116 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.116 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215669 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64700.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150968 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215669 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23475e-08, 215669 } } kg +compflowStatistics: Max phase CFL number: 5.98517 +compflowStatistics: Max component CFL number: 162.768 +Time: 5.03233e+06s, dt:61012.1s, Cycle: 160 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 6.70e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 6.23e-08 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 4.91e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-04 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 1.74e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.167529 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0394896 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.09334e+06s, dt:86002.2s, Cycle: 161 +well_1Control: BHP (at the specified reference elevation): 25211920.033206165 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 6.55e-08 ) ; ( R ) = ( 3.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.42e-07 ) ; ( R ) = ( 4.23e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 6.21e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.70e-07 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 4.82e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.234735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0554318 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.17934e+06s, dt:99856.9s, Cycle: 162 +well_1Control: BHP (at the specified reference elevation): 25274266.443245966 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 6.46e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.76e-07 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 7.15e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 7.43e-08 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 4.39e-08 ) ; ( R ) = ( 9.88e-03 ) ; + Last LinSolve(iter,res) = ( 10, 6.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 6.54e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.270517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636705 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.2792e+06s, dt:106262s, Cycle: 163 +well_1Control: BHP (at the specified reference elevation): 25346212.50093299 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 6.40e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.73e-07 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 7.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.51e-05 ) ; ( Rwell ) = ( 5.43e-15 ) ; ( R ) = ( 3.51e-05 ) ; + Last LinSolve(iter,res) = ( 10, 6.22e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25422499.70661009 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.285479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065458 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.38546e+06s, dt:111067s, Cycle: 164 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 6.36e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 5.85e-07 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 11, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.18e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 11, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.76e-05 ) ; ( Rwell ) = ( 1.60e-14 ) ; ( R ) = ( 4.76e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.295746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667561 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.49653e+06s, dt:114608s, Cycle: 165 +well_1Control: BHP (at the specified reference elevation): 25501689.04174665 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 6.29e-08 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 4.55e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 9.21e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 6.83e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.17e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25583048.26835718 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.302369 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687938 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.61114e+06s, dt:115940s, Cycle: 166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 6.24e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 7.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.09e-07 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 4.45e-13 ) ; ( R ) = ( 6.38e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.30304 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681258 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.72708e+06s, dt:118047s, Cycle: 167 +well_1Control: BHP (at the specified reference elevation): 25664950.489428356 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 6.18e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.37e-07 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 7.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.13e-07 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-05 ) ; ( Rwell ) = ( 2.37e-15 ) ; ( R ) = ( 1.34e-05 ) ; + Last LinSolve(iter,res) = ( 12, 3.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.30568 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675652 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.84512e+06s, dt:120849s, Cycle: 168 +well_1Control: BHP (at the specified reference elevation): 25748041.565993454 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 6.14e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.93e-07 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 7.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.46e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.00e-06 ) ; ( Rwell ) = ( 3.59e-15 ) ; ( R ) = ( 1.00e-06 ) ; + Last LinSolve(iter,res) = ( 14, 1.08e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25832433.366695642 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.310001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691058 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.96597e+06s, dt:34027.1s, Cycle: 169 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 6.06e-08 ) ; ( R ) = ( 1.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-04 ) ; ( Rwell ) = ( 3.75e-11 ) ; ( R ) = ( 2.40e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.086863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0194668 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6e+06s, dt:65596.7s, Cycle: 170 +well_1Control: BHP (at the specified reference elevation): 25856913.25142446 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 6.24e-08 ) ; ( R ) = ( 2.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 5.54e-08 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.13e-11 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-05 ) ; ( Rwell ) = ( 9.33e-15 ) ; ( R ) = ( 2.41e-05 ) ; + Last LinSolve(iter,res) = ( 9, 3.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.166764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0369916 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.50737e+07, 1.51151e+07, 1.52341e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.55017e+06, 2.71078e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.635 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.02874, 726.607 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1432.19, 702716 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 213.352, 211995 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1218.84, 490722 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.126, 0.0676278 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1430.07, 702716 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1432.19, 0 }, { 361.23, 702348 } } kg +well_1Control: BHP (at the specified reference elevation): 25902985.002441168 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.46972e+07, 1.49663e+07, 1.50922e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.17272e+06, 2.56866e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.201 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.201 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215813 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64744 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151069 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215813 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23625e-08, 215813 } } kg +compflowStatistics: Max phase CFL number: 11.5128 +compflowStatistics: Max component CFL number: 318.883 +Time: 6.0656e+06s, dt:95673s, Cycle: 171 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 6.08e-08 ) ; ( R ) = ( 3.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 2.75e-07 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 6.33e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.98e-05 ) ; ( Rwell ) = ( 3.50e-15 ) ; ( R ) = ( 1.98e-05 ) ; + Last LinSolve(iter,res) = ( 10, 5.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.241724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.16127e+06s, dt:112366s, Cycle: 172 +well_1Control: BHP (at the specified reference elevation): 25969223.99680371 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 5.97e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 2.03e-07 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 11, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 6.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.83e-05 ) ; ( Rwell ) = ( 4.65e-15 ) ; ( R ) = ( 3.83e-05 ) ; + Last LinSolve(iter,res) = ( 11, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.281688 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636614 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.27364e+06s, dt:119585s, Cycle: 173 +well_1Control: BHP (at the specified reference elevation): 26046642.557964556 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 5.49e-07 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 12, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 7.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 4.86e-07 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 7.01e-12 ) ; ( R ) = ( 9.21e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.297191 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664293 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.39322e+06s, dt:123795s, Cycle: 174 +well_1Control: BHP (at the specified reference elevation): 26128617.12281309 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 6.11e-07 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.83e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 1.06e-12 ) ; ( R ) = ( 8.24e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.304859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660474 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.51701e+06s, dt:128637s, Cycle: 175 +well_1Control: BHP (at the specified reference elevation): 26213023.49331142 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 5.43e-07 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.08e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.72e-04 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 4.72e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.07e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26300299.677630812 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.64565e+06s, dt:132419s, Cycle: 176 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 4.89e-07 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.50e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 7.58e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.319936 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696076 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.77807e+06s, dt:132915s, Cycle: 177 +well_1Control: BHP (at the specified reference elevation): 26389434.31894476 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 5.69e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 4.24e-07 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 9.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.29e-13 ) ; ( R ) = ( 6.87e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.318055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670378 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.91099e+06s, dt:89014s, Cycle: 178 +well_1Control: BHP (at the specified reference elevation): 26478635.21409888 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 5.65e-08 ) ; ( R ) = ( 2.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 3.05e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26538776.676723607 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.211455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0460961 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7e+06s, dt:115252s, Cycle: 179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 5.67e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.23e-07 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-04 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 3.22e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.271816 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0595847 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.54367e+07, 1.54781e+07, 1.55949e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.89758e+06, 3.05596e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.899 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.59307, 726.306 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1688.84, 702632 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 251.434, 212135 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1437.4, 490497 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.51594, 0.0676077 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1686.32, 702632 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1688.84, 0 }, { 414.933, 702208 } } kg +well_1Control: BHP (at the specified reference elevation): 26615547.486276664 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.50778e+07, 1.53342e+07, 1.54552e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.53695e+06, 2.91609e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.283 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.283 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215953 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64785.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151167 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215953 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23769e-08, 215953 } } kg +compflowStatistics: Max phase CFL number: 398.11 +compflowStatistics: Max component CFL number: 542.04 +Time: 7.11525e+06s, dt:127943s, Cycle: 180 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 5.57e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.09e-07 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.20e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 4.63e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26700071.939514957 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299224 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065187 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.24319e+06s, dt:134089s, Cycle: 181 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 5.50e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 4.55e-07 ) ; ( R ) = ( 5.04e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.57e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 6.50e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.310784 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637148 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.37728e+06s, dt:142627s, Cycle: 182 +well_1Control: BHP (at the specified reference elevation): 26788221.72422655 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 5.45e-08 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.38e-07 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 1.21e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.96e-05 ) ; ( Rwell ) = ( 3.03e-15 ) ; ( R ) = ( 1.96e-05 ) ; + Last LinSolve(iter,res) = ( 11, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.327431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701329 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.51991e+06s, dt:142446s, Cycle: 183 +well_1Control: BHP (at the specified reference elevation): 26881413.160952218 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.94e-07 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 9.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.94e-06 ) ; ( Rwell ) = ( 4.35e-16 ) ; ( R ) = ( 9.94e-06 ) ; + Last LinSolve(iter,res) = ( 12, 4.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.323883 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682963 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.66236e+06s, dt:144796s, Cycle: 184 +well_1Control: BHP (at the specified reference elevation): 26973992.27192258 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 3.64e-07 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 6.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.55e-07 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 4.69e-15 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 11, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.326086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695309 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.80715e+06s, dt:145446s, Cycle: 185 +well_1Control: BHP (at the specified reference elevation): 27067601.94973743 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 4.65e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 6.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.26e-07 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.51e-06 ) ; ( Rwell ) = ( 3.53e-15 ) ; ( R ) = ( 7.51e-06 ) ; + Last LinSolve(iter,res) = ( 12, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.324458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660865 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.9526e+06s, dt:47401.4s, Cycle: 186 +well_1Control: BHP (at the specified reference elevation): 27161137.349176176 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; ( R ) = ( 1.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.32e-13 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-05 ) ; ( Rwell ) = ( 2.93e-17 ) ; ( R ) = ( 1.87e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.105193 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.022483 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8e+06s, dt:86584.6s, Cycle: 187 +well_1Control: BHP (at the specified reference elevation): 27192245.799220264 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 5.33e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.02e-05 ) ; ( Rwell ) = ( 2.69e-15 ) ; ( R ) = ( 4.02e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.11e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27248031.92419106 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.191313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.040172 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.57592e+07, 1.58005e+07, 1.59157e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.23071e+06, 3.38735e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.134 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.09333, 726.04 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1927.84, 702557 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 286.718, 212260 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1641.12, 490298 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.77175, 0.338749 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1925.07, 702557 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1927.84, 0 }, { 463.125, 702084 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.5414e+07, 1.56603e+07, 1.57777e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.88456e+06, 3.24923e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.355 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.355 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216077 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64823 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151254 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216077 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23898e-08, 216077 } } kg +compflowStatistics: Max phase CFL number: 290.53 +compflowStatistics: Max component CFL number: 395.843 +Time: 8.08658e+06s, dt:120941s, Cycle: 188 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 6.29e-08 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 7.88e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.265493 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0564405 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.20753e+06s, dt:138875s, Cycle: 189 +well_1Control: BHP (at the specified reference elevation): 27324775.052664313 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 5.12e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 1.15e-15 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 11, 7.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27412524.813789345 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.302384 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064737 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.3464e+06s, dt:146203s, Cycle: 190 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 5.08e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 4.93e-07 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 11, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 2.35e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.15e-06 ) ; ( Rwell ) = ( 1.05e-15 ) ; ( R ) = ( 9.15e-06 ) ; + Last LinSolve(iter,res) = ( 11, 7.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.315506 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661781 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.4926e+06s, dt:151726s, Cycle: 191 +well_1Control: BHP (at the specified reference elevation): 27504503.008631535 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 4.73e-07 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 2.11e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.43e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.63e-06 ) ; ( Rwell ) = ( 1.38e-16 ) ; ( R ) = ( 5.63e-06 ) ; + Last LinSolve(iter,res) = ( 11, 9.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.324397 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671326 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.64433e+06s, dt:155986s, Cycle: 192 +well_1Control: BHP (at the specified reference elevation): 27599375.06387212 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 4.60e-07 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 1.98e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.56e-05 ) ; ( Rwell ) = ( 1.08e-15 ) ; ( R ) = ( 1.56e-05 ) ; + Last LinSolve(iter,res) = ( 12, 6.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.330348 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691257 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.80032e+06s, dt:157295s, Cycle: 193 +well_1Control: BHP (at the specified reference elevation): 27696247.19256337 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.92e-08 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 4.43e-07 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.89e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.49e-06 ) ; ( Rwell ) = ( 6.28e-16 ) ; ( R ) = ( 6.49e-06 ) ; + Last LinSolve(iter,res) = ( 12, 6.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.32998 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682022 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.95761e+06s, dt:42389.2s, Cycle: 194 +well_1Control: BHP (at the specified reference elevation): 27793532.8333307 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 1.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.09e-03 ) ; ( Rwell ) = ( 5.03e-08 ) ; ( R ) = ( 7.09e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-04 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 1.33e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0884903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0181471 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9e+06s, dt:83746.1s, Cycle: 195 +well_1Control: BHP (at the specified reference elevation): 27820281.70071256 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 2.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-05 ) ; ( Rwell ) = ( 3.87e-16 ) ; ( R ) = ( 1.25e-05 ) ; + Last LinSolve(iter,res) = ( 10, 2.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.174154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0372013 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.60782e+07, 1.61194e+07, 1.62333e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.55165e+06, 3.70682e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.365 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.58711, 725.778 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2174.17, 702484 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 323.143, 212383 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1851.03, 490101 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.99397, 0.338836 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2171.18, 702484 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2174.17, 0 }, { 511.625, 701962 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.57455e+07, 1.59828e+07, 1.60968e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.21809e+06, 3.57017e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.427 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.427 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216199 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64859.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151339 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216199 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24024e-08, 216199 } } kg +well_1Control: BHP (at the specified reference elevation): 27872169.85774828 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 273.31 +compflowStatistics: Max component CFL number: 372.652 +Time: 9.08375e+06s, dt:121789s, Cycle: 196 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.17e-07 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.79e-05 ) ; ( Rwell ) = ( 9.08e-16 ) ; ( R ) = ( 4.79e-05 ) ; + Last LinSolve(iter,res) = ( 11, 4.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27946758.31573136 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.25178 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0526165 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.20554e+06s, dt:145953s, Cycle: 197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.79e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.09e-07 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 1.36e-07 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.28e-06 ) ; ( Rwell ) = ( 6.73e-15 ) ; ( R ) = ( 8.28e-06 ) ; + Last LinSolve(iter,res) = ( 11, 8.48e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28035476.629097365 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637866 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.35149e+06s, dt:155133s, Cycle: 198 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 1.99e-07 ) ; ( R ) = ( 4.37e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 5.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.22e-07 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 6.70e-15 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 11, 9.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.315479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662594 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.50662e+06s, dt:160864s, Cycle: 199 +well_1Control: BHP (at the specified reference elevation): 28129390.909110084 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 1.98e-07 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 1.53e-15 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 12, 7.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.324164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674475 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.66748e+06s, dt:164872s, Cycle: 200 +well_1Control: BHP (at the specified reference elevation): 28226148.966519635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 1.99e-07 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.08e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 3.17e-16 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 12, 7.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28324872.52647619 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.329191 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674513 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.83236e+06s, dt:167644s, Cycle: 201 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 2.00e-07 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 5.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.18e-07 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.57e-06 ) ; ( Rwell ) = ( 2.37e-15 ) ; ( R ) = ( 6.57e-06 ) ; + Last LinSolve(iter,res) = ( 12, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.331642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664991 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1e+07s, dt:173426s, Cycle: 202 +well_1Control: BHP (at the specified reference elevation): 28424567.732968584 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.12e-07 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 5.27e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.30e-07 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.84e-06 ) ; ( Rwell ) = ( 8.12e-15 ) ; ( R ) = ( 7.84e-06 ) ; + Last LinSolve(iter,res) = ( 12, 8.86e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28527188.452097714 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.339898 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685686 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.64143e+07, 1.64554e+07, 1.6568e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.86159e+06, 4.01548e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.61 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.10575, 725.504 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2443.86, 702409 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 363.534, 212513 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2080.33, 489896 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 3.47631, 0.338944 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2440.39, 702409 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2443.86, 0 }, { 564.115, 701833 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.60938e+07, 1.63224e+07, 1.64329e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.53927e+06, 3.88011e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.502 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.502 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216328 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64898.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151429 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216328 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24158e-08, 216328 } } kg +compflowStatistics: Max phase CFL number: 550.232 +compflowStatistics: Max component CFL number: 750.794 +Time: 1.01734e+07s, dt:175823s, Cycle: 203 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.23e-07 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 9.71e-12 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-05 ) ; ( Rwell ) = ( 9.25e-16 ) ; ( R ) = ( 1.83e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.341369 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677114 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03492e+07s, dt:179741s, Cycle: 204 +well_1Control: BHP (at the specified reference elevation): 28630419.41902359 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.37e-07 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.56e-07 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 4.49e-13 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.00e-05 ) ; ( Rwell ) = ( 6.35e-16 ) ; ( R ) = ( 2.00e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.14e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28735420.97012584 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345702 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701293 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.0529e+07s, dt:179520s, Cycle: 205 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.44e-07 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 5.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.90e-05 ) ; ( Rwell ) = ( 5.36e-16 ) ; ( R ) = ( 2.90e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.342039 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688185 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.07085e+07s, dt:181563s, Cycle: 206 +well_1Control: BHP (at the specified reference elevation): 28839469.605180867 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.33e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.54e-07 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 13, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 7.08e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 2.78e-13 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.53e-06 ) ; ( Rwell ) = ( 2.66e-16 ) ; ( R ) = ( 5.53e-06 ) ; + Last LinSolve(iter,res) = ( 13, 7.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.342773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682504 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08901e+07s, dt:109927s, Cycle: 207 +well_1Control: BHP (at the specified reference elevation): 28944451.826230098 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-05 ) ; ( Rwell ) = ( 1.27e-15 ) ; ( R ) = ( 2.14e-05 ) ; + Last LinSolve(iter,res) = ( 10, 3.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.206171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0418813 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.1e+07s, dt:150132s, Cycle: 208 +well_1Control: BHP (at the specified reference elevation): 29008381.807242304 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; ( R ) = ( 3.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 6.46e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 1.73e-15 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 11, 7.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29094450.886851575 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279845 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0572214 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.67068e+07, 1.67478e+07, 1.68595e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.16229e+06, 4.31519e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.822 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.55654, 725.266 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2687.09, 702344 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 399.569, 212626 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2287.52, 489718 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 3.60181, 0.47701 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2683.48, 702344 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2687.09, 0 }, { 609.676, 701722 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.63951e+07, 1.66171e+07, 1.67253e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.84935e+06, 4.18082e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.567 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.567 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216439 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64931.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151508 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216439 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24274e-08, 216439 } } kg +compflowStatistics: Max phase CFL number: 465.167 +compflowStatistics: Max component CFL number: 635.113 +Time: 1.11501e+07s, dt:170935s, Cycle: 209 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 6.04e-08 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 10, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.78e-06 ) ; ( Rwell ) = ( 1.15e-15 ) ; ( R ) = ( 7.78e-06 ) ; + Last LinSolve(iter,res) = ( 12, 7.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.316144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064111 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13211e+07s, dt:181092s, Cycle: 210 +well_1Control: BHP (at the specified reference elevation): 29191447.589675263 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 13, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 7.14e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-05 ) ; ( Rwell ) = ( 1.43e-15 ) ; ( R ) = ( 1.10e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.19e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29293811.180370715 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663383 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15022e+07s, dt:187635s, Cycle: 211 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 4.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.51e-07 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 8.62e-08 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.98e-05 ) ; ( Rwell ) = ( 4.31e-15 ) ; ( R ) = ( 2.98e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.340972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067545 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.16898e+07s, dt:192127s, Cycle: 212 +well_1Control: BHP (at the specified reference elevation): 29399259.642532744 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 1.67e-07 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.29e-05 ) ; ( Rwell ) = ( 1.35e-15 ) ; ( R ) = ( 1.29e-05 ) ; + Last LinSolve(iter,res) = ( 13, 7.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.345986 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682947 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18819e+07s, dt:118078s, Cycle: 213 +well_1Control: BHP (at the specified reference elevation): 29506606.975592315 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 5.46e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 8.14e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.211222 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.042412 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2e+07s, dt:160159s, Cycle: 214 +well_1Control: BHP (at the specified reference elevation): 29572818.258222587 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 6.32e-08 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.77e-13 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.38e-06 ) ; ( Rwell ) = ( 5.86e-16 ) ; ( R ) = ( 9.38e-06 ) ; + Last LinSolve(iter,res) = ( 12, 7.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.284668 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.056899 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 29661484.72851167 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.70007e+07, 1.70417e+07, 1.71526e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.45464e+06, 4.60667e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.036 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.00871, 725.027 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2939.09, 702280 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 436.893, 212740 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2502.2, 489540 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 4.01913, 0.477146 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2935.07, 702279 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2939.09, 0 }, { 656.303, 701609 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.66976e+07, 1.69135e+07, 1.70193e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.15019e+06, 4.47318e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.633 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.633 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216552 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64965.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151586 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216552 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2439e-08, 216552 } } kg +compflowStatistics: Max phase CFL number: 484.941 +compflowStatistics: Max component CFL number: 662.496 +Time: 1.21602e+07s, dt:182991s, Cycle: 215 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 6.24e-13 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.91e-06 ) ; ( Rwell ) = ( 1.51e-16 ) ; ( R ) = ( 3.91e-06 ) ; + Last LinSolve(iter,res) = ( 13, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.322697 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645261 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.23431e+07s, dt:193056s, Cycle: 216 +well_1Control: BHP (at the specified reference elevation): 29762166.142481238 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 4.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 9.99e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 5.00e-16 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 13, 7.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.337531 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661237 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25362e+07s, dt:200456s, Cycle: 217 +well_1Control: BHP (at the specified reference elevation): 29867744.69249519 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.18e-07 ) ; ( R ) = ( 4.25e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 6.40e-08 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.41e-05 ) ; ( Rwell ) = ( 6.11e-15 ) ; ( R ) = ( 2.41e-05 ) ; + Last LinSolve(iter,res) = ( 14, 8.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.347374 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068232 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27367e+07s, dt:203889s, Cycle: 218 +well_1Control: BHP (at the specified reference elevation): 29976761.23543067 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 4.24e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 7.95e-08 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-05 ) ; ( Rwell ) = ( 4.86e-17 ) ; ( R ) = ( 1.34e-05 ) ; + Last LinSolve(iter,res) = ( 13, 7.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.35018 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29405e+07s, dt:59450s, Cycle: 219 +well_1Control: BHP (at the specified reference elevation): 30086957.148764852 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; ( R ) = ( 1.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 6.46e-09 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.51e-03 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 8.33e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.92e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.72e-03 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-03 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.56e-03 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 7.84e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.70e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 7.77e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.59e-03 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.87e-05 ) ; ( Rwell ) = ( 1.64e-13 ) ; ( R ) = ( 4.87e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.101596 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0201832 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.3e+07s, dt:113119s, Cycle: 220 +well_1Control: BHP (at the specified reference elevation): 30119565.848637234 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; ( R ) = ( 2.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 7.53e-08 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 3.95e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.192628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0374108 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.72716e+07, 1.73125e+07, 1.74228e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.73956e+06, 4.89088e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.233 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.42487, 724.808 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3177.88, 702220 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 472.31, 212845 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2705.57, 489375 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 4.32211, 0.477276 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3173.56, 702220 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3177.88, 0 }, { 699.275, 701506 } } kg +well_1Control: BHP (at the specified reference elevation): 30180707.699304365 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.69753e+07, 1.71861e+07, 1.72901e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.44266e+06, 4.7581e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.694 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.694 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216655 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64996.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151659 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216655 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24497e-08, 216655 } } kg +compflowStatistics: Max phase CFL number: 335.561 +compflowStatistics: Max component CFL number: 458.653 +Time: 1.31131e+07s, dt:164029s, Cycle: 221 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 8.28e-08 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-06 ) ; ( Rwell ) = ( 8.66e-15 ) ; ( R ) = ( 1.90e-06 ) ; + Last LinSolve(iter,res) = ( 13, 6.24e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30268425.49909646 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.277732 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0555367 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32771e+07s, dt:190233s, Cycle: 222 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 3.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 9.76e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.02e-05 ) ; ( Rwell ) = ( 2.38e-15 ) ; ( R ) = ( 2.02e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.319683 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637012 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34674e+07s, dt:202373s, Cycle: 223 +well_1Control: BHP (at the specified reference elevation): 30369489.668137465 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 3.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 6.77e-08 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 6.68e-13 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.36e-05 ) ; ( Rwell ) = ( 7.72e-16 ) ; ( R ) = ( 3.36e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.337276 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662052 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36698e+07s, dt:209961s, Cycle: 224 +well_1Control: BHP (at the specified reference elevation): 30476579.680349257 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 16, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 16, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-05 ) ; ( Rwell ) = ( 2.66e-16 ) ; ( R ) = ( 1.47e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.346873 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663829 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38797e+07s, dt:120285s, Cycle: 225 +well_1Control: BHP (at the specified reference elevation): 30586720.61521007 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; ( R ) = ( 2.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.23e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.58e-06 ) ; ( Rwell ) = ( 1.61e-15 ) ; ( R ) = ( 4.58e-06 ) ; + Last LinSolve(iter,res) = ( 11, 2.80e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30650325.596415386 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.197486 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0385824 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4e+07s, dt:171643s, Cycle: 226 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 3.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.00e-05 ) ; ( Rwell ) = ( 1.34e-15 ) ; ( R ) = ( 1.00e-05 ) ; + Last LinSolve(iter,res) = ( 12, 7.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.280202 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561074 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75653e+07, 1.76061e+07, 1.77159e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.01805e+06, 5.16874e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.446 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.87539, 724.571 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3443.57, 702157 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 512.009, 212959 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2931.56, 489198 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 4.48527, 0.477417 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3439.08, 702156 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3443.57, 0 }, { 746.561, 701394 } } kg +well_1Control: BHP (at the specified reference elevation): 30739929.14501611 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.72761e+07, 1.74819e+07, 1.75838e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.72785e+06, 5.0366e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.76 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.76 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216767 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65030.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151737 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216767 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24613e-08, 216767 } } kg +compflowStatistics: Max phase CFL number: 498.36 +compflowStatistics: Max component CFL number: 681.517 +Time: 1.41716e+07s, dt:197817s, Cycle: 227 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; ( R ) = ( 3.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 6.97e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.59e-05 ) ; ( Rwell ) = ( 3.76e-15 ) ; ( R ) = ( 1.59e-05 ) ; + Last LinSolve(iter,res) = ( 14, 8.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.320575 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623514 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43695e+07s, dt:213359s, Cycle: 228 +well_1Control: BHP (at the specified reference elevation): 30842363.955798488 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 8.10e-08 ) ; ( R ) = ( 4.02e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 16, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.50e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.13e-05 ) ; ( Rwell ) = ( 6.89e-16 ) ; ( R ) = ( 2.13e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.342907 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673799 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45828e+07s, dt:218819s, Cycle: 229 +well_1Control: BHP (at the specified reference elevation): 30952120.52839476 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 3.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 8.60e-08 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 17, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 9.29e-13 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 11, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-05 ) ; ( Rwell ) = ( 7.13e-16 ) ; ( R ) = ( 1.90e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.348644 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066962 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48016e+07s, dt:198362s, Cycle: 230 +well_1Control: BHP (at the specified reference elevation): 31063995.87138772 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 3.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 7.43e-08 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 9.34e-09 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 8.86e-13 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-05 ) ; ( Rwell ) = ( 1.20e-17 ) ; ( R ) = ( 1.19e-05 ) ; + Last LinSolve(iter,res) = ( 13, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.313591 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0609137 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5e+07s, dt:217154s, Cycle: 231 +well_1Control: BHP (at the specified reference elevation): 31165367.71224309 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; ( R ) = ( 3.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 8.00e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 8.05e-13 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-05 ) ; ( Rwell ) = ( 1.45e-16 ) ; ( R ) = ( 1.34e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.340636 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653894 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78486e+07, 1.78894e+07, 1.79987e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29028e+06, 5.44043e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.652 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 8.30887, 724.343 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3706.07, 702096 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.242, 213069 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 3154.83, 489028 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.09207, 0.477553 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3700.98, 702096 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3706.07, 0 }, { 793.185, 701286 } } kg +well_1Control: BHP (at the specified reference elevation): 31275275.527124807 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.75659e+07, 1.77671e+07, 1.78672e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00629e+06, 5.30883e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.823 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.823 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216875 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65062.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151813 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216875 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24725e-08, 216875 } } kg +compflowStatistics: Max phase CFL number: 618.035 +compflowStatistics: Max component CFL number: 845.562 +Time: 1.52172e+07s, dt:227127s, Cycle: 232 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 8.67e-08 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.52e-12 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.11e-05 ) ; ( Rwell ) = ( 1.11e-16 ) ; ( R ) = ( 2.11e-05 ) ; + Last LinSolve(iter,res) = ( 13, 9.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.353355 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679083 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54443e+07s, dt:231744s, Cycle: 233 +well_1Control: BHP (at the specified reference elevation): 31389558.754781567 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 15, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-05 ) ; ( Rwell ) = ( 3.14e-15 ) ; ( R ) = ( 1.65e-05 ) ; + Last LinSolve(iter,res) = ( 13, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.357546 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691701 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5676e+07s, dt:233590s, Cycle: 234 +well_1Control: BHP (at the specified reference elevation): 31505521.05788015 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 3.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-05 ) ; ( Rwell ) = ( 2.20e-16 ) ; ( R ) = ( 9.11e-05 ) ; + Last LinSolve(iter,res) = ( 13, 9.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.357408 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676329 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59096e+07s, dt:90385.4s, Cycle: 235 +well_1Control: BHP (at the specified reference elevation): 31621631.558648437 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; ( R ) = ( 1.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 6.93e-09 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 8.36e-13 ) ; ( R ) = ( 9.92e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.88e-05 ) ; ( Rwell ) = ( 1.50e-15 ) ; ( R ) = ( 5.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.137582 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0275183 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6e+07s, dt:151803s, Cycle: 236 +well_1Control: BHP (at the specified reference elevation): 31667105.292515587 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.58e-09 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 9.11e-10 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.39e-04 ) ; ( Rwell ) = ( 4.54e-13 ) ; ( R ) = ( 4.39e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.230206 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0452875 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.80978e+07, 1.81386e+07, 1.82475e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.55748e+06, 5.70722e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.833 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 8.69028, 724.143 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3942.2, 702043 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 586.25, 213165 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 3355.95, 488878 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.26276, 0.477671 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3936.94, 702042 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3942.2, 0 }, { 833.4, 701191 } } kg +well_1Control: BHP (at the specified reference elevation): 31742411.544289846 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.78196e+07, 1.80174e+07, 1.81164e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27868e+06, 5.57604e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.878 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.878 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 216970 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65091 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151879 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216970 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24823e-08, 216970 } } kg +compflowStatistics: Max phase CFL number: 424.776 +compflowStatistics: Max component CFL number: 581.377 +Time: 1.61518e+07s, dt:198528s, Cycle: 237 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; ( R ) = ( 3.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 1.57e-14 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.42e-06 ) ; ( Rwell ) = ( 1.24e-15 ) ; ( R ) = ( 7.42e-06 ) ; + Last LinSolve(iter,res) = ( 12, 8.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 31839848.222748302 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299315 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575797 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.63503e+07s, dt:225162s, Cycle: 238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.15e-13 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.16e-05 ) ; ( Rwell ) = ( 7.81e-16 ) ; ( R ) = ( 2.16e-05 ) ; + Last LinSolve(iter,res) = ( 12, 8.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.336975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664116 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.65755e+07s, dt:233129s, Cycle: 239 +well_1Control: BHP (at the specified reference elevation): 31949804.09899024 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.30e-12 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.74e-05 ) ; ( Rwell ) = ( 1.11e-15 ) ; ( R ) = ( 1.74e-05 ) ; + Last LinSolve(iter,res) = ( 15, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.346119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689039 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.68086e+07s, dt:191378s, Cycle: 240 +well_1Control: BHP (at the specified reference elevation): 32062968.539077006 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; ( R ) = ( 3.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 9.87e-09 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.66e-05 ) ; ( Rwell ) = ( 1.88e-15 ) ; ( R ) = ( 3.66e-05 ) ; + Last LinSolve(iter,res) = ( 11, 8.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.282168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0570495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.7e+07s, dt:218303s, Cycle: 241 +well_1Control: BHP (at the specified reference elevation): 32155789.41477418 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; ( R ) = ( 3.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 8.23e-09 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 5.33e-09 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 8.40e-13 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 2.08e-15 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 12, 8.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.319714 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061422 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.83766e+07, 1.84173e+07, 1.85258e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.81989e+06, 5.96923e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 733.036 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 9.11597, 723.92 } rm^3 +compflowStatistics, reservoir: Phase mass: { 4211.43, 701984 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 626.424, 213273 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 3585.01, 488711 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.65852, 0.750174 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 4205.77, 701983 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 4211.43, 0 }, { 879.503, 701085 } } kg +well_1Control: BHP (at the specified reference elevation): 32260807.70910906 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.81037e+07, 1.82977e+07, 1.83951e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.54602e+06, 5.83845e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.941 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.941 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217076 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65122.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151953 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217076 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.24933e-08, 217076 } } kg +compflowStatistics: Max phase CFL number: 599.763 +compflowStatistics: Max component CFL number: 821.198 +Time: 1.72183e+07s, dt:237724s, Cycle: 242 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 5.08e-09 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-05 ) ; ( Rwell ) = ( 7.23e-16 ) ; ( R ) = ( 1.82e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.345552 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674222 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.7456e+07s, dt:243707s, Cycle: 243 +well_1Control: BHP (at the specified reference elevation): 32374416.845970377 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 3.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 9.85e-09 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 16, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.11e-13 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 4.91e-16 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 14, 6.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.351442 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679554 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.76997e+07s, dt:248547s, Cycle: 244 +well_1Control: BHP (at the specified reference elevation): 32490108.602498177 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; ( R ) = ( 3.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 6.24e-09 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.38e-14 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-05 ) ; ( Rwell ) = ( 3.22e-16 ) ; ( R ) = ( 1.85e-05 ) ; + Last LinSolve(iter,res) = ( 14, 8.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.355613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669969 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.79483e+07s, dt:51720.1s, Cycle: 245 +well_1Control: BHP (at the specified reference elevation): 32607610.80849405 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 6.25e-10 ) ; ( R ) = ( 9.01e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 1.59e-10 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 1.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.23e-10 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.08e-10 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.64e-05 ) ; ( Rwell ) = ( 8.92e-14 ) ; ( R ) = ( 3.64e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0736773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0143781 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.8e+07s, dt:103440s, Cycle: 246 +well_1Control: BHP (at the specified reference elevation): 32632441.908762015 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; ( R ) = ( 1.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 4.75e-10 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 1.98e-13 ) ; ( R ) = ( 7.18e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.147053 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0295936 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.86047e+07, 1.86454e+07, 1.87537e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 6.07792e+06, 6.22698e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 733.202 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 9.46434, 723.737 } rm^3 +compflowStatistics, reservoir: Phase mass: { 4435.92, 701935 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 659.58, 213361 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 3776.34, 488574 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.67921, 0.750328 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 4430.24, 701934 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 4435.92, 0 }, { 916.726, 700998 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.83353e+07, 1.85267e+07, 1.86232e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.80842e+06, 6.09649e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.992 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.992 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217163 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65148.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152014 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217163 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25023e-08, 217163 } } kg +well_1Control: BHP (at the specified reference elevation): 32681600.941451803 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 280.098 +compflowStatistics: Max component CFL number: 383.627 +Time: 1.81034e+07s, dt:168147s, Cycle: 247 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-05 ) ; ( Rwell ) = ( 2.50e-15 ) ; ( R ) = ( 4.65e-05 ) ; + Last LinSolve(iter,res) = ( 10, 9.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.238176 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0466182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.82716e+07s, dt:216318s, Cycle: 248 +well_1Control: BHP (at the specified reference elevation): 32760449.888274647 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; ( R ) = ( 3.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.28e-10 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 9.73e-14 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.70e-06 ) ; ( Rwell ) = ( 5.98e-16 ) ; ( R ) = ( 9.70e-06 ) ; + Last LinSolve(iter,res) = ( 13, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.304633 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601537 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.84879e+07s, dt:238702s, Cycle: 249 +well_1Control: BHP (at the specified reference elevation): 32861204.728381097 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.05e-12 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.54e-05 ) ; ( Rwell ) = ( 1.20e-15 ) ; ( R ) = ( 2.54e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.333723 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652919 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.87266e+07s, dt:249907s, Cycle: 250 +well_1Control: BHP (at the specified reference elevation): 32971695.69800196 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.94e-13 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.68e-05 ) ; ( Rwell ) = ( 1.57e-15 ) ; ( R ) = ( 1.68e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.346731 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685489 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.89765e+07s, dt:23485.8s, Cycle: 251 +well_1Control: BHP (at the specified reference elevation): 33086909.886766095 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.75e-08 ) ; ( R ) = ( 3.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.60e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 3.40e-14 ) ; ( R ) = ( 8.75e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0327189 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00652556 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.9e+07s, dt:46971.7s, Cycle: 252 +well_1Control: BHP (at the specified reference elevation): 33097956.695160158 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 2.80e-08 ) ; ( R ) = ( 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.96e-10 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 4.78e-11 ) ; ( R ) = ( 6.38e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.23e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.29e-05 ) ; ( Rwell ) = ( 2.54e-14 ) ; ( R ) = ( 6.29e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0648516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0128836 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.88442e+07, 1.88849e+07, 1.89929e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 6.3321e+06, 6.48089e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 733.376 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 9.82948, 723.546 } rm^3 +compflowStatistics, reservoir: Phase mass: { 4675.17, 701885 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 695.067, 213454 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 3980.11, 488431 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 6.14139, 0.750489 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 4669.03, 701884 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 4675.17, 0 }, { 956.445, 700907 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.85787e+07, 1.87673e+07, 1.88627e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 6.06669e+06, 6.35067e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.045 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.045 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217254 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65176.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152078 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217254 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25118e-08, 217254 } } kg +well_1Control: BHP (at the specified reference elevation): 33119941.10359099 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 125.328 +compflowStatistics: Max component CFL number: 171.701 +Time: 1.9047e+07s, dt:93943.4s, Cycle: 253 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; ( R ) = ( 1.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-05 ) ; ( Rwell ) = ( 6.84e-16 ) ; ( R ) = ( 2.48e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.129483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0262357 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.91409e+07s, dt:161084s, Cycle: 254 +well_1Control: BHP (at the specified reference elevation): 33163482.477113653 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; ( R ) = ( 2.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 6.97e-09 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 8.69e-09 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 1.37e-12 ) ; ( R ) = ( 5.24e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.22133 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0432863 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9302e+07s, dt:216050s, Cycle: 255 +well_1Control: BHP (at the specified reference elevation): 33237283.41027396 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; ( R ) = ( 3.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.75e-06 ) ; ( Rwell ) = ( 1.11e-15 ) ; ( R ) = ( 5.75e-06 ) ; + Last LinSolve(iter,res) = ( 13, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.295251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0597241 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9518e+07s, dt:239488s, Cycle: 256 +well_1Control: BHP (at the specified reference elevation): 33335490.98890602 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; ( R ) = ( 3.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-05 ) ; ( Rwell ) = ( 1.02e-15 ) ; ( R ) = ( 2.33e-05 ) ; + Last LinSolve(iter,res) = ( 14, 9.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.325017 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636577 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.97575e+07s, dt:242463s, Cycle: 257 +well_1Control: BHP (at the specified reference elevation): 33443794.157643512 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; ( R ) = ( 3.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 9.64e-11 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.03e-05 ) ; ( Rwell ) = ( 1.55e-15 ) ; ( R ) = ( 1.03e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.326725 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646837 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2e+07s, dt:255394s, Cycle: 258 +well_1Control: BHP (at the specified reference elevation): 33553122.29116211 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 6.72e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.14e-14 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.98e-05 ) ; ( Rwell ) = ( 1.37e-16 ) ; ( R ) = ( 1.98e-05 ) ; + Last LinSolve(iter,res) = ( 13, 9.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 33667447.47012551 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341657 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645334 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.91461e+07, 1.91868e+07, 1.92946e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 6.58279e+06, 6.73135e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 733.595 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 10.2891, 723.306 } rm^3 +compflowStatistics, reservoir: Phase mass: { 4981.82, 701822 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 740.607, 213571 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 4241.22, 488251 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 6.19432, 1.29535 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 4975.63, 701820 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 4981.82, 0 }, { 1007.09, 700792 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.88854e+07, 1.90707e+07, 1.91647e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 6.32107e+06, 6.60136e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.112 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.112 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217369 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65210.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152158 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217369 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25237e-08, 217369 } } kg +compflowStatistics: Max phase CFL number: 669.312 +compflowStatistics: Max component CFL number: 917.292 +Time: 2.02554e+07s, dt:269421s, Cycle: 259 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; ( R ) = ( 3.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.13e-07 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 17, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 17, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 9.78e-14 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-05 ) ; ( Rwell ) = ( 9.38e-16 ) ; ( R ) = ( 1.16e-05 ) ; + Last LinSolve(iter,res) = ( 15, 8.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 33787383.50426074 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357716 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696858 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.05248e+07s, dt:270230s, Cycle: 260 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 17, 8.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-04 ) ; ( Rwell ) = ( 1.78e-15 ) ; ( R ) = ( 1.03e-04 ) ; + Last LinSolve(iter,res) = ( 12, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.356139 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674039 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.0795e+07s, dt:204955s, Cycle: 261 +well_1Control: BHP (at the specified reference elevation): 33907124.30237386 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; ( R ) = ( 2.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 5.12e-08 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 8.60e-10 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.54e-13 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-05 ) ; ( Rwell ) = ( 4.22e-17 ) ; ( R ) = ( 1.19e-05 ) ; + Last LinSolve(iter,res) = ( 12, 7.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.268488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0514042 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.1e+07s, dt:249065s, Cycle: 262 +well_1Control: BHP (at the specified reference elevation): 33997880.220615774 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; ( R ) = ( 3.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 7.41e-08 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.08e-14 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.59e-06 ) ; ( Rwell ) = ( 3.46e-17 ) ; ( R ) = ( 3.59e-06 ) ; + Last LinSolve(iter,res) = ( 15, 7.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.324373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627048 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.93909e+07, 1.94315e+07, 1.95392e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 6.82988e+06, 6.97826e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 733.773 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 10.6613, 723.112 } rm^3 +compflowStatistics, reservoir: Phase mass: { 5234.4, 701771 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 778.016, 213666 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 4456.38, 488105 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 6.61368, 1.57833 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 5227.79, 701769 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 5234.4, 0 }, { 1048.31, 700699 } } kg +well_1Control: BHP (at the specified reference elevation): 34107105.24999443 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.91334e+07, 1.93163e+07, 1.94095e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 6.5715e+06, 6.84845e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.167 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.167 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217462 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65238.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152223 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217462 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25333e-08, 217462 } } kg +compflowStatistics: Max phase CFL number: 643.637 +compflowStatistics: Max component CFL number: 882.336 +Time: 2.12491e+07s, dt:267662s, Cycle: 263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; ( R ) = ( 3.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 3.99e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 7.00e-13 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 6.42e-17 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 16, 6.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.346194 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660305 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.15167e+07s, dt:278178s, Cycle: 264 +well_1Control: BHP (at the specified reference elevation): 34223748.112712495 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; ( R ) = ( 3.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; ( R ) = ( 3.95e-02 ) ; + Last LinSolve(iter,res) = ( 17, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 9.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 18, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.45e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 12, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 7.65e-16 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 15, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.357263 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068633 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17949e+07s, dt:205095s, Cycle: 265 +well_1Control: BHP (at the specified reference elevation): 34344511.593512736 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 13, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 3.92e-15 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.19e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 34433493.58144771 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.261876 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0496618 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.2e+07s, dt:254365s, Cycle: 266 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; ( R ) = ( 3.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 7.60e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 8.32e-13 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-05 ) ; ( Rwell ) = ( 1.43e-15 ) ; ( R ) = ( 1.21e-05 ) ; + Last LinSolve(iter,res) = ( 14, 8.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.322992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626461 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.96356e+07, 1.96762e+07, 1.97838e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 7.07401e+06, 7.22225e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 733.951 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 11.0331, 722.918 } rm^3 +compflowStatistics, reservoir: Phase mass: { 5490.36, 701720 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 815.909, 213761 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 4674.45, 487959 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 6.91947, 1.57864 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 5483.44, 701719 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 5490.36, 0 }, { 1089.59, 700606 } } kg +well_1Control: BHP (at the specified reference elevation): 34542827.94266162 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.9381e+07, 1.95619e+07, 1.96542e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 6.81865e+06, 7.09259e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.221 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.221 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217555 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65266.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152288 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217555 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25429e-08, 217555 } } kg +compflowStatistics: Max phase CFL number: 648.477 +compflowStatistics: Max component CFL number: 889.187 +Time: 2.22544e+07s, dt:273521s, Cycle: 267 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; ( R ) = ( 3.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 17, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 17, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.20e-13 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 12, 8.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-06 ) ; ( Rwell ) = ( 1.86e-16 ) ; ( R ) = ( 3.39e-06 ) ; + Last LinSolve(iter,res) = ( 17, 3.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.34503 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666723 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.25279e+07s, dt:282473s, Cycle: 268 +well_1Control: BHP (at the specified reference elevation): 34659714.95009595 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.87e-07 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 17, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 6.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 18, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.58e-06 ) ; ( Rwell ) = ( 1.56e-15 ) ; ( R ) = ( 8.58e-06 ) ; + Last LinSolve(iter,res) = ( 15, 7.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.353903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675898 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.28104e+07s, dt:189640s, Cycle: 269 +well_1Control: BHP (at the specified reference elevation): 34779912.02008939 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; ( R ) = ( 2.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 9.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 9.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.57e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 6.23e-15 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 11, 9.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.236306 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0452608 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.3e+07s, dt:248094s, Cycle: 270 +well_1Control: BHP (at the specified reference elevation): 34860610.26390748 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; ( R ) = ( 2.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 6.07e-08 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 4.14e-15 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 15, 8.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.307629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059198 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 34965294.69515199 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.9875e+07, 1.99156e+07, 2.00231e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 7.31548e+06, 7.46361e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 734.125 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 11.3966, 722.728 } rm^3 +compflowStatistics, reservoir: Phase mass: { 5743.97, 701671 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 853.38, 213854 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 4890.59, 487817 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 7.50943, 1.57895 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 5736.46, 701669 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 5743.97, 0 }, { 1129.79, 700515 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.9623e+07, 1.9802e+07, 1.98936e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 7.06286e+06, 7.33406e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.275 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.275 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217646 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65293.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152352 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217646 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25524e-08, 217646 } } kg +compflowStatistics: Max phase CFL number: 624.424 +compflowStatistics: Max component CFL number: 856.394 +Time: 2.32481e+07s, dt:276544s, Cycle: 271 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 3.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 18, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 18, 6.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.24e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 12, 8.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 1.28e-15 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 16, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.340778 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638972 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.35246e+07s, dt:293610s, Cycle: 272 +well_1Control: BHP (at the specified reference elevation): 35081236.800372 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; ( R ) = ( 3.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 19, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 19, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 4.85e-13 ) ; ( R ) = ( 7.37e-04 ) ; + Last LinSolve(iter,res) = ( 13, 8.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.359329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675115 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.38182e+07s, dt:181752s, Cycle: 273 +well_1Control: BHP (at the specified reference elevation): 35203662.95621306 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; ( R ) = ( 3.10e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.21e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; ( R ) = ( 9.21e-03 ) ; + Last LinSolve(iter,res) = ( 12, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.54e-06 ) ; ( Rwell ) = ( 2.94e-16 ) ; ( R ) = ( 1.54e-06 ) ; + Last LinSolve(iter,res) = ( 12, 6.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.221241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0420961 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.4e+07s, dt:247534s, Cycle: 274 +well_1Control: BHP (at the specified reference elevation): 35279534.871154875 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; ( R ) = ( 2.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-05 ) ; ( Rwell ) = ( 7.77e-16 ) ; ( R ) = ( 1.90e-05 ) ; + Last LinSolve(iter,res) = ( 14, 9.73e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 35382074.0783085 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299931 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557178 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.01132e+07, 2.01538e+07, 2.02612e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 7.55441e+06, 7.70245e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 734.298 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 11.7581, 722.54 } rm^3 +compflowStatistics, reservoir: Phase mass: { 5999.27, 701622 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 890.992, 213946 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 5108.28, 487676 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 7.97615, 1.57927 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 5991.3, 701620 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 5999.27, 0 }, { 1169.99, 700425 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.98638e+07, 2.00409e+07, 2.01318e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 7.30439e+06, 7.57299e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.328 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.328 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217736 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65320.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152415 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217736 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25617e-08, 217736 } } kg +compflowStatistics: Max phase CFL number: 615.353 +compflowStatistics: Max component CFL number: 844.125 +Time: 2.42475e+07s, dt:286505s, Cycle: 275 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; ( R ) = ( 3.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 8.54e-08 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 18, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 7.19e-08 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 18, 9.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.13e-13 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.78e-06 ) ; ( Rwell ) = ( 2.46e-16 ) ; ( R ) = ( 7.78e-06 ) ; + Last LinSolve(iter,res) = ( 16, 7.21e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 35499939.05427738 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643393 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.4534e+07s, dt:302831s, Cycle: 276 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 1.38e-07 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 19, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 19, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 4.24e-13 ) ; ( R ) = ( 9.58e-04 ) ; + Last LinSolve(iter,res) = ( 14, 7.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.362202 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.48369e+07s, dt:163130s, Cycle: 277 +well_1Control: BHP (at the specified reference elevation): 35623783.913642064 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; ( R ) = ( 1.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.82e-06 ) ; ( Rwell ) = ( 1.89e-15 ) ; ( R ) = ( 7.82e-06 ) ; + Last LinSolve(iter,res) = ( 11, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.194132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0363018 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.5e+07s, dt:240227s, Cycle: 278 +well_1Control: BHP (at the specified reference elevation): 35690797.9078668 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 1.21e-07 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.96e-13 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 12, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.28e-06 ) ; ( Rwell ) = ( 4.10e-16 ) ; ( R ) = ( 5.28e-06 ) ; + Last LinSolve(iter,res) = ( 14, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.284737 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0525531 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.03475e+07, 2.03881e+07, 2.04955e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 7.79101e+06, 7.93899e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 734.468 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 12.1134, 722.355 } rm^3 +compflowStatistics, reservoir: Phase mass: { 6253.19, 701573 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 928.189, 214037 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 5325, 487536 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 8.09801, 1.57956 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 6245.09, 701572 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 6253.19, 0 }, { 1209.59, 700336 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.01004e+07, 2.02759e+07, 2.03661e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 7.54336e+06, 7.8096e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.38 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.38 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217825 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65347.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152478 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217825 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25709e-08, 217825 } } kg +well_1Control: BHP (at the specified reference elevation): 35788515.785403535 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 590.188 +compflowStatistics: Max component CFL number: 809.751 +Time: 2.52402e+07s, dt:288098s, Cycle: 279 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; ( R ) = ( 3.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.99e-07 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 18, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 6.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 18, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 1.18e-14 ) ; ( R ) = ( 6.09e-04 ) ; + Last LinSolve(iter,res) = ( 13, 7.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.339518 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631988 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.55283e+07s, dt:308051s, Cycle: 280 +well_1Control: BHP (at the specified reference elevation): 35904942.19485366 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 20, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 9.09e-08 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 20, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.51e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 14, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.10e-06 ) ; ( Rwell ) = ( 2.52e-16 ) ; ( R ) = ( 8.10e-06 ) ; + Last LinSolve(iter,res) = ( 18, 4.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.360633 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0680657 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.58364e+07s, dt:163624s, Cycle: 281 +well_1Control: BHP (at the specified reference elevation): 36028761.06349833 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; ( R ) = ( 1.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.61e-05 ) ; ( Rwell ) = ( 4.17e-15 ) ; ( R ) = ( 2.61e-05 ) ; + Last LinSolve(iter,res) = ( 10, 8.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.190615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0353396 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.6e+07s, dt:244251s, Cycle: 282 +well_1Control: BHP (at the specified reference elevation): 36094797.21416174 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; ( R ) = ( 2.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 8.93e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.43e-14 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 12, 7.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-05 ) ; ( Rwell ) = ( 1.06e-15 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 13, 9.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.283403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051786 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.05823e+07, 2.06229e+07, 2.07303e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 8.02544e+06, 8.17338e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 734.639 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 12.4691, 722.17 } rm^3 +compflowStatistics, reservoir: Phase mass: { 6510.19, 701525 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 965.648, 214128 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 5544.54, 487397 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 8.29836, 1.57987 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 6501.89, 701523 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 6510.19, 0 }, { 1249.45, 700247 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.03375e+07, 2.05113e+07, 2.06009e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 7.77999e+06, 8.04403e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.432 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.432 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 217914 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65374.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152540 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 217914 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25802e-08, 217914 } } kg +well_1Control: BHP (at the specified reference elevation): 36192303.94334931 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 593.242 +compflowStatistics: Max component CFL number: 814.083 +Time: 2.62443e+07s, dt:295513s, Cycle: 283 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.42e-07 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 19, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 6.74e-09 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 19, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 6.00e-13 ) ; ( R ) = ( 7.56e-04 ) ; + Last LinSolve(iter,res) = ( 13, 8.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.340902 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624136 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.65398e+07s, dt:318527s, Cycle: 284 +well_1Control: BHP (at the specified reference elevation): 36309602.98764027 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; ( R ) = ( 3.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 2.59e-07 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 20, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 8.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 6.35e-08 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 20, 9.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 4.41e-04 ) ; + Last LinSolve(iter,res) = ( 15, 8.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.365035 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661261 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.68583e+07s, dt:141710s, Cycle: 285 +well_1Control: BHP (at the specified reference elevation): 36435436.49969533 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 1.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.87e-04 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 3.87e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.161655 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0300377 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.7e+07s, dt:228783s, Cycle: 286 +well_1Control: BHP (at the specified reference elevation): 36491831.02423525 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.06e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 8.06e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.02e-05 ) ; ( Rwell ) = ( 1.98e-15 ) ; ( R ) = ( 4.02e-05 ) ; + Last LinSolve(iter,res) = ( 12, 8.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.260181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0483815 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.08108e+07, 2.08513e+07, 2.09587e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 8.2578e+06, 8.40571e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 734.805 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 12.8151, 721.99 } rm^3 +compflowStatistics, reservoir: Phase mass: { 6762.74, 701478 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1002.74, 214216 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 5760, 487262 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 8.65581, 1.58016 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 6754.08, 701476 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 6762.74, 0 }, { 1287.99, 700160 } } kg +well_1Control: BHP (at the specified reference elevation): 36581874.91353764 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.05678e+07, 2.07402e+07, 2.08294e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 8.0144e+06, 8.27639e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.483 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.483 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218001 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65400.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152601 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218001 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25892e-08, 218001 } } kg +compflowStatistics: Max phase CFL number: 549.704 +compflowStatistics: Max component CFL number: 754.449 +Time: 2.72288e+07s, dt:288100s, Cycle: 287 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 3.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 8.42e-08 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 18, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 6.88e-08 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 18, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 1.28e-12 ) ; ( R ) = ( 8.03e-04 ) ; + Last LinSolve(iter,res) = ( 13, 9.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.325944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593522 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.75169e+07s, dt:320613s, Cycle: 288 +well_1Control: BHP (at the specified reference elevation): 36694314.46731789 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 21, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 8.27e-09 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 21, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 6.00e-13 ) ; ( R ) = ( 8.25e-04 ) ; + Last LinSolve(iter,res) = ( 15, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.360435 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648921 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.78375e+07s, dt:162503s, Cycle: 289 +well_1Control: BHP (at the specified reference elevation): 36818943.50382728 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; ( R ) = ( 1.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 9.85e-08 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 8.10e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.181825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0329462 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.8e+07s, dt:251123s, Cycle: 290 +well_1Control: BHP (at the specified reference elevation): 36882399.3239393 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 1.28e-07 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 5.15e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.50e-13 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 12, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 1.38e-15 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.279985 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.05192 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.10459e+07, 2.10865e+07, 2.11938e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 8.48831e+06, 8.63621e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 734.976 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 13.171, 721.805 } rm^3 +compflowStatistics, reservoir: Phase mass: { 7025.02, 701430 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1040.98, 214307 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 5984.04, 487122 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 9.3664, 1.58046 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 7015.65, 701428 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 7025.02, 0 }, { 1327.98, 700071 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.08049e+07, 2.0976e+07, 2.10645e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 8.24684e+06, 8.50691e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.536 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.536 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218090 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65427 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152663 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218090 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.25984e-08, 218090 } } kg +well_1Control: BHP (at the specified reference elevation): 36979524.11362441 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 596.906 +compflowStatistics: Max component CFL number: 819.353 +Time: 2.82511e+07s, dt:303358s, Cycle: 291 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.16e-07 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 18, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 6.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 18, 8.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 3.84e-13 ) ; ( R ) = ( 7.18e-04 ) ; + Last LinSolve(iter,res) = ( 13, 8.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.336383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612681 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.85545e+07s, dt:330874s, Cycle: 292 +well_1Control: BHP (at the specified reference elevation): 37096048.27490966 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.28e-07 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 20, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.49e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 8.68e-09 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 20, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 1.12e-12 ) ; ( R ) = ( 8.19e-03 ) ; + Last LinSolve(iter,res) = ( 14, 8.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.06e-04 ) ; ( Rwell ) = ( 1.30e-15 ) ; ( R ) = ( 1.06e-04 ) ; + Last LinSolve(iter,res) = ( 16, 8.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 37222485.07957494 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.364541 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642541 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.88854e+07s, dt:114646s, Cycle: 293 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; ( R ) = ( 1.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 2.67e-10 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 7.70e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.56e-10 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.42e-05 ) ; ( Rwell ) = ( 1.02e-13 ) ; ( R ) = ( 3.42e-05 ) ; + Last LinSolve(iter,res) = ( 10, 5.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.12576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0225503 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.9e+07s, dt:209170s, Cycle: 294 +well_1Control: BHP (at the specified reference elevation): 37266719.76832829 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; ( R ) = ( 2.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 10, 9.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.42e-05 ) ; ( Rwell ) = ( 3.60e-15 ) ; ( R ) = ( 2.42e-05 ) ; + Last LinSolve(iter,res) = ( 12, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.228889 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0428992 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 37346450.55611834 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.12647e+07, 2.13052e+07, 2.14126e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 8.71701e+06, 8.86491e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 735.135 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 13.5018, 721.633 } rm^3 +compflowStatistics, reservoir: Phase mass: { 7271.09, 701385 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1076.46, 214392 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 6194.62, 486993 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 9.75405, 2.1284 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 7261.33, 701383 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 7271.09, 0 }, { 1365.19, 699988 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.10254e+07, 2.11952e+07, 2.12833e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 8.47736e+06, 8.73561e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.584 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.584 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218173 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65451.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152721 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218173 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2607e-08, 218173 } } kg +compflowStatistics: Max phase CFL number: 492.369 +compflowStatistics: Max component CFL number: 675.942 +Time: 2.92092e+07s, dt:281940s, Cycle: 295 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; ( R ) = ( 3.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 8.98e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 13, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-05 ) ; ( Rwell ) = ( 1.66e-14 ) ; ( R ) = ( 2.25e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.307126 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0559569 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.94911e+07s, dt:325469s, Cycle: 296 +well_1Control: BHP (at the specified reference elevation): 37453137.630541325 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.57e-07 ) ; ( R ) = ( 3.17e-02 ) ; + Last LinSolve(iter,res) = ( 19, 9.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.89e-10 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.21e-05 ) ; ( Rwell ) = ( 1.43e-13 ) ; ( R ) = ( 5.21e-05 ) ; + Last LinSolve(iter,res) = ( 20, 7.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.352455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633732 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.98166e+07s, dt:183421s, Cycle: 297 +well_1Control: BHP (at the specified reference elevation): 37575787.63691229 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 8.01e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 1.18e-12 ) ; ( R ) = ( 7.56e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.197725 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0350996 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3e+07s, dt:274741s, Cycle: 298 +well_1Control: BHP (at the specified reference elevation): 37645248.734723605 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.67e-07 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 5.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.80e-13 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 1.42e-17 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 14, 9.64e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 37748227.773838595 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.295081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0550567 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.15062e+07, 2.15467e+07, 2.16541e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 8.94412e+06, 9.09204e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 735.311 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 13.8667, 721.444 } rm^3 +compflowStatistics, reservoir: Phase mass: { 7544.96, 701336 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1116.6, 214486 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 6428.36, 486850 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 10.3744, 2.40207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 7534.59, 701333 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 7544.96, 0 }, { 1406.36, 699897 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.12687e+07, 2.14372e+07, 2.15248e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 8.70613e+06, 8.96272e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.638 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.638 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218264 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65479.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152785 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218264 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26165e-08, 218264 } } kg +compflowStatistics: Max phase CFL number: 640.002 +compflowStatistics: Max component CFL number: 878.735 +Time: 3.02747e+07s, dt:320329s, Cycle: 299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 9.51e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 19, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 6.37e-03 ) ; + Last LinSolve(iter,res) = ( 14, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.56e-05 ) ; ( Rwell ) = ( 1.98e-14 ) ; ( R ) = ( 7.56e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.3421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0615452 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.05951e+07s, dt:348381s, Cycle: 300 +well_1Control: BHP (at the specified reference elevation): 37867385.42984527 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 3.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 1.80e-07 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 20, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 16, 7.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.29e-05 ) ; ( Rwell ) = ( 2.52e-15 ) ; ( R ) = ( 7.29e-05 ) ; + Last LinSolve(iter,res) = ( 13, 7.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.369746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645264 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.09435e+07s, dt:56548.8s, Cycle: 301 +well_1Control: BHP (at the specified reference elevation): 37996617.471553326 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-05 ) ; ( Rwell ) = ( 6.98e-14 ) ; ( R ) = ( 2.63e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0600116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0105508 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.1e+07s, dt:113098s, Cycle: 302 +well_1Control: BHP (at the specified reference elevation): 38017894.134117804 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 1.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.15e-09 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 7.81e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-04 ) ; ( Rwell ) = ( 1.35e-13 ) ; ( R ) = ( 1.48e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.119441 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0210234 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.16952e+07, 2.17357e+07, 2.18431e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 9.16948e+06, 9.31743e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 735.448 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 14.1523, 721.296 } rm^3 +compflowStatistics, reservoir: Phase mass: { 7760.9, 701297 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1148.06, 214559 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 6612.84, 486738 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 10.9894, 2.75453 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 7749.91, 701294 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 7760.9, 0 }, { 1438.31, 699825 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.14588e+07, 2.16264e+07, 2.17138e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 8.93317e+06, 9.18809e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.68 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.68 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218336 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65500.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152835 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218336 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26239e-08, 218336 } } kg +well_1Control: BHP (at the specified reference elevation): 38060171.53020831 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 261.374 +compflowStatistics: Max component CFL number: 358.905 +Time: 3.11131e+07s, dt:211969s, Cycle: 303 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; ( R ) = ( 2.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.61e-04 ) ; ( Rwell ) = ( 8.87e-13 ) ; ( R ) = ( 3.61e-04 ) ; + Last LinSolve(iter,res) = ( 11, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.223469 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0411632 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.13251e+07s, dt:292225s, Cycle: 304 +well_1Control: BHP (at the specified reference elevation): 38138605.02009622 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; ( R ) = ( 2.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 17, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 6.02e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.42e-05 ) ; ( Rwell ) = ( 1.95e-14 ) ; ( R ) = ( 6.42e-05 ) ; + Last LinSolve(iter,res) = ( 14, 7.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.306797 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0555029 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.16173e+07s, dt:339035s, Cycle: 305 +well_1Control: BHP (at the specified reference elevation): 38245832.89394217 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 3.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 20, 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.37e-11 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-04 ) ; ( Rwell ) = ( 2.94e-14 ) ; ( R ) = ( 3.43e-04 ) ; + Last LinSolve(iter,res) = ( 14, 8.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 38369424.57242135 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.353741 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0625477 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.19563e+07s, dt:43673.9s, Cycle: 306 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 6.22e-10 ) ; ( R ) = ( 6.28e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.56e-10 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.38e-10 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 9.44e-11 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 8.30e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 7.30e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 6.41e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 5.65e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.52e-06 ) ; ( Rwell ) = ( 6.01e-14 ) ; ( R ) = ( 4.52e-06 ) ; + Last LinSolve(iter,res) = ( 8, 5.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0455209 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00806674 +Time: 3.2e+07s, dt:43673.9s, Cycle: 307 +well_1Control: BHP (at the specified reference elevation): 38385587.896808356 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 4.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.29e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; ( R ) = ( 8.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-05 ) ; ( Rwell ) = ( 1.06e-12 ) ; ( R ) = ( 2.03e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.045356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00811698 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.19035e+07, 2.1944e+07, 2.20515e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 9.39362e+06, 9.5416e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 735.599 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 14.4667, 721.133 } rm^3 +compflowStatistics, reservoir: Phase mass: { 8000.39, 701255 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1182.19, 214640 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 6818.2, 486615 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 11.3938, 2.75495 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 7989, 701252 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 8000.39, 0 }, { 1473.96, 699746 } } kg +well_1Control: BHP (at the specified reference elevation): 38401749.65273344 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.16687e+07, 2.18352e+07, 2.19221e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 9.15885e+06, 9.41222e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.726 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.726 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218415 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65524.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152890 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218415 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26321e-08, 218415 } } kg +compflowStatistics: Max phase CFL number: 100.075 +compflowStatistics: Max component CFL number: 137.43 +Time: 3.20437e+07s, dt:87347.8s, Cycle: 308 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.68e-03 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 8.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; ( R ) = ( 7.61e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 3.25e-13 ) ; ( R ) = ( 4.98e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0906432 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0161059 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.2131e+07s, dt:174696s, Cycle: 309 +well_1Control: BHP (at the specified reference elevation): 38433902.84871943 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 1.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.23e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 5.43e-10 ) ; ( R ) = ( 7.15e-03 ) ; + Last LinSolve(iter,res) = ( 10, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.69e-05 ) ; ( Rwell ) = ( 2.72e-13 ) ; ( R ) = ( 9.69e-05 ) ; + Last LinSolve(iter,res) = ( 10, 9.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 38497740.40337254 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.181059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0327032 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.23057e+07s, dt:270933s, Cycle: 310 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 7.25e-08 ) ; ( R ) = ( 3.80e-02 ) ; + Last LinSolve(iter,res) = ( 15, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 9.48e-04 ) ; + Last LinSolve(iter,res) = ( 12, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.279866 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051888 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.25767e+07s, dt:327410s, Cycle: 311 +well_1Control: BHP (at the specified reference elevation): 38595891.48704187 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 3.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 1.37e-07 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 19, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 2.37e-11 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-04 ) ; ( Rwell ) = ( 3.46e-14 ) ; ( R ) = ( 2.47e-04 ) ; + Last LinSolve(iter,res) = ( 14, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.336337 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598043 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.29041e+07s, dt:95940.1s, Cycle: 312 +well_1Control: BHP (at the specified reference elevation): 38713803.61549186 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 1.56e-08 ) ; ( R ) = ( 9.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.39e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 7.34e-10 ) ; ( R ) = ( 6.83e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 4.98e-14 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0981631 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0174706 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.3e+07s, dt:191880s, Cycle: 313 +well_1Control: BHP (at the specified reference elevation): 38748694.07120996 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 1.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 7.60e-12 ) ; ( R ) = ( 4.48e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.195952 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0346964 +compflowStatistics, reservoir: Pressure (min, average, max): 2.21594e+07, 2.21998e+07, 2.23074e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 9.61666e+06, 9.76469e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 735.785 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 14.8534, 720.932 } rm^3 +compflowStatistics, reservoir: Phase mass: { 8297.01, 701202 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1224.57, 214739 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 7072.44, 486463 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 12.079, 2.75547 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 8284.93, 701199 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 8297.01, 0 }, { 1516.83, 699649 } } kg +well_1Control: BHP (at the specified reference elevation): 38817872.41292214 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.1926e+07, 2.20915e+07, 2.2178e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 9.38313e+06, 9.63527e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.783 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.783 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218512 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65553.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 152958 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218512 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26421e-08, 218512 } } kg +compflowStatistics: Max phase CFL number: 435.222 +compflowStatistics: Max component CFL number: 597.744 +Time: 3.31919e+07s, dt:191880s, Cycle: 314 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 1.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 7.61e-10 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.18e-04 ) ; ( Rwell ) = ( 6.12e-11 ) ; ( R ) = ( 3.18e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.195393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0351889 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.33838e+07s, dt:287046s, Cycle: 315 +well_1Control: BHP (at the specified reference elevation): 38886844.19062619 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 2.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 5.59e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.04e-05 ) ; ( Rwell ) = ( 8.94e-15 ) ; ( R ) = ( 3.04e-05 ) ; + Last LinSolve(iter,res) = ( 13, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.29116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0535416 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.36708e+07s, dt:329194s, Cycle: 316 +well_1Control: BHP (at the specified reference elevation): 38989285.68591801 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 3.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.18e-07 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 19, 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 15, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 1.91e-15 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 15, 6.59e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 39106142.65115763 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593447 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.4e+07s, dt:366373s, Cycle: 317 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.37e-07 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 22, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.69e-11 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 17, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.54e-05 ) ; ( Rwell ) = ( 2.58e-14 ) ; ( R ) = ( 3.54e-05 ) ; + Last LinSolve(iter,res) = ( 13, 8.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.367309 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638294 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.24185e+07, 2.2459e+07, 2.25666e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 9.83792e+06, 9.98599e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 735.974 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 15.2434, 720.73 } rm^3 +compflowStatistics, reservoir: Phase mass: { 8598.99, 701150 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1268.61, 214839 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 7330.38, 486311 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 13.0496, 3.10304 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 8585.94, 701147 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 8598.99, 0 }, { 1562.11, 699551 } } kg +well_1Control: BHP (at the specified reference elevation): 39235763.10494584 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.21872e+07, 2.23514e+07, 2.24372e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 9.60598e+06, 9.85652e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.841 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.841 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218610 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65583 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153027 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218610 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26523e-08, 218610 } } kg +compflowStatistics: Max phase CFL number: 822.745 +compflowStatistics: Max component CFL number: 1130.09 +Time: 3.43664e+07s, dt:389248s, Cycle: 318 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; ( R ) = ( 3.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.71e-07 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 23, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 18, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-04 ) ; ( Rwell ) = ( 8.60e-15 ) ; ( R ) = ( 1.09e-04 ) ; + Last LinSolve(iter,res) = ( 14, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.387815 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670066 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.47556e+07s, dt:244379s, Cycle: 319 +well_1Control: BHP (at the specified reference elevation): 39372858.88226179 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; ( R ) = ( 2.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; ( R ) = ( 4.22e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 8.68e-04 ) ; + Last LinSolve(iter,res) = ( 12, 9.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.242314 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0428941 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.5e+07s, dt:329420s, Cycle: 320 +well_1Control: BHP (at the specified reference elevation): 39459094.01416783 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 9.73e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 20, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.65e-12 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.51e-12 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 14, 8.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 1.44e-15 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 16, 7.08e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 39574250.56838216 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.325304 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557142 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.26301e+07, 2.26706e+07, 2.27783e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.0058e+07, 1.02061e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 736.128 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 15.5621, 720.566 } rm^3 +compflowStatistics, reservoir: Phase mass: { 8847.43, 701107 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1304.03, 214921 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 7543.4, 486186 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 13.1604, 3.38741 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 8834.27, 701104 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 8847.43, 0 }, { 1598.41, 699471 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.23998e+07, 2.25632e+07, 2.26488e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 9.82719e+06, 1.00766e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.888 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.888 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218690 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65607 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153083 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218690 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26606e-08, 218690 } } kg +compflowStatistics: Max phase CFL number: 733.924 +compflowStatistics: Max component CFL number: 1008.16 +Time: 3.53294e+07s, dt:381297s, Cycle: 321 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 3.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 2.11e-07 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 22, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.40e-11 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 18, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.28e-05 ) ; ( Rwell ) = ( 2.47e-14 ) ; ( R ) = ( 7.28e-05 ) ; + Last LinSolve(iter,res) = ( 15, 9.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.374438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064434 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.57107e+07s, dt:289283s, Cycle: 322 +well_1Control: BHP (at the specified reference elevation): 39706907.60235628 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 2.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 8.25e-08 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 17, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 13, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.94e-05 ) ; ( Rwell ) = ( 4.97e-15 ) ; ( R ) = ( 3.94e-05 ) ; + Last LinSolve(iter,res) = ( 14, 8.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.282709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0482358 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.6e+07s, dt:364924s, Cycle: 323 +well_1Control: BHP (at the specified reference elevation): 39807670.33951118 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 22, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 3.24e-14 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 15, 7.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 39933685.320176944 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354961 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613606 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.28564e+07, 2.28969e+07, 2.30047e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.02769e+07, 1.04251e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 736.292 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 15.9027, 720.389 } rm^3 +compflowStatistics, reservoir: Phase mass: { 9114.66, 701062 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1342.29, 215009 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 7772.37, 486053 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 13.6006, 3.38797 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 9101.06, 701058 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 9114.66, 0 }, { 1637.35, 699385 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.26273e+07, 2.27899e+07, 2.28751e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.00473e+07, 1.02955e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.938 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.938 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218776 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65632.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153143 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218776 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26695e-08, 218776 } } kg +compflowStatistics: Max phase CFL number: 806.344 +compflowStatistics: Max component CFL number: 1107.72 +Time: 3.63649e+07s, dt:397641s, Cycle: 324 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 1.38e-07 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 23, 8.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 6.94e-03 ) ; + Last LinSolve(iter,res) = ( 18, 9.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 1.06e-14 ) ; ( R ) = ( 4.06e-04 ) ; + Last LinSolve(iter,res) = ( 15, 9.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 40070209.312602535 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.384455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064889 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.67626e+07s, dt:237435s, Cycle: 325 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 2.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 14, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.99e-12 ) ; ( R ) = ( 4.18e-04 ) ; + Last LinSolve(iter,res) = ( 12, 8.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.228484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0380728 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.7e+07s, dt:341175s, Cycle: 326 +well_1Control: BHP (at the specified reference elevation): 40151986.02475265 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 3.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.23e-07 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 20, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 3.33e-11 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 15, 9.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-04 ) ; ( Rwell ) = ( 9.91e-15 ) ; ( R ) = ( 1.82e-04 ) ; + Last LinSolve(iter,res) = ( 16, 6.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.327138 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0554101 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.30688e+07, 2.31093e+07, 2.32172e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.04947e+07, 1.0643e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 736.447 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 16.2224, 720.224 } rm^3 +compflowStatistics, reservoir: Phase mass: { 9367.02, 701018 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1378.27, 215091 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 7988.74, 485927 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 14.8088, 3.38848 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 9352.21, 701015 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 9367.02, 0 }, { 1673.64, 699305 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.28407e+07, 2.30025e+07, 2.30875e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.02662e+07, 1.05133e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 224.986 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 224.986 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218856 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65656.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153199 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218856 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26778e-08, 218856 } } kg +well_1Control: BHP (at the specified reference elevation): 40268662.864167824 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s +compflowStatistics: Max phase CFL number: 748.206 +compflowStatistics: Max component CFL number: 1027.91 +Time: 3.73412e+07s, dt:396233s, Cycle: 327 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 3.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.66e-07 ) ; ( R ) = ( 3.17e-02 ) ; + Last LinSolve(iter,res) = ( 23, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.28e-11 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 8.68e-15 ) ; ( R ) = ( 4.09e-04 ) ; + Last LinSolve(iter,res) = ( 21, 8.12e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 40403227.61016985 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.377849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.77374e+07s, dt:262592s, Cycle: 328 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 2.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 8.60e-04 ) ; + Last LinSolve(iter,res) = ( 12, 9.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.249207 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0418519 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.8e+07s, dt:358770s, Cycle: 329 +well_1Control: BHP (at the specified reference elevation): 40492523.421988636 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 3.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.18e-07 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 19, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 8.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 5.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 8.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 9.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.89e-05 ) ; ( Rwell ) = ( 2.76e-14 ) ; ( R ) = ( 3.89e-05 ) ; + Last LinSolve(iter,res) = ( 18, 8.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.339069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0571423 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.32891e+07, 2.33296e+07, 2.34375e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.07116e+07, 1.086e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 736.607 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 16.5536, 720.053 } rm^3 +compflowStatistics, reservoir: Phase mass: { 9629.99, 700974 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1415.48, 215176 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 8214.51, 485798 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 15.2236, 3.66374 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 9614.76, 700970 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 9629.99, 0 }, { 1711.54, 699221 } } kg +well_1Control: BHP (at the specified reference elevation): 40613635.23128869 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.3062e+07, 2.32231e+07, 2.33077e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.04841e+07, 1.07302e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.035 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.035 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 218940 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65681.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153258 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 218940 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26864e-08, 218940 } } kg +compflowStatistics: Max phase CFL number: 780.816 +compflowStatistics: Max component CFL number: 1072.77 +Time: 3.83588e+07s, dt:408833s, Cycle: 330 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 2.66e-07 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 21, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 4.26e-11 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.90e-05 ) ; ( Rwell ) = ( 1.28e-14 ) ; ( R ) = ( 3.90e-05 ) ; + Last LinSolve(iter,res) = ( 16, 6.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.384248 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663838 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.87676e+07s, dt:232397s, Cycle: 331 +well_1Control: BHP (at the specified reference elevation): 40751004.73097582 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 2.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 7.14e-08 ) ; ( R ) = ( 3.48e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-04 ) ; ( Rwell ) = ( 6.85e-13 ) ; ( R ) = ( 2.37e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.217453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0370843 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.9e+07s, dt:338516s, Cycle: 332 +well_1Control: BHP (at the specified reference elevation): 40829335.88218635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 3.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 1.37e-07 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 18, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 6.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.19e-13 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.89e-04 ) ; ( Rwell ) = ( 1.39e-15 ) ; ( R ) = ( 1.89e-04 ) ; + Last LinSolve(iter,res) = ( 14, 9.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.315664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.053511 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.35004e+07, 2.35409e+07, 2.36489e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.09276e+07, 1.1076e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 736.76 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 16.8718, 719.888 } rm^3 +compflowStatistics, reservoir: Phase mass: { 9883.91, 700931 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1451.41, 215258 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 8432.49, 485673 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 15.5284, 3.66429 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 9868.38, 700927 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 9883.91, 0 }, { 1747.31, 699141 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.32742e+07, 2.34347e+07, 2.35191e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.0701e+07, 1.09462e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.082 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.082 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219020 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65705.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153314 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219020 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.26947e-08, 219020 } } kg +well_1Control: BHP (at the specified reference elevation): 40942466.72767274 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 731.5 +compflowStatistics: Max component CFL number: 1005.06 +Time: 3.93385e+07s, dt:401579s, Cycle: 333 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 21, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 16, 8.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-05 ) ; ( Rwell ) = ( 3.73e-14 ) ; ( R ) = ( 3.26e-05 ) ; + Last LinSolve(iter,res) = ( 22, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.372494 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618809 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.97401e+07s, dt:259905s, Cycle: 334 +well_1Control: BHP (at the specified reference elevation): 41075911.77594389 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 2.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 13, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 5.18e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.239974 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0405559 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4e+07s, dt:361190s, Cycle: 335 +well_1Control: BHP (at the specified reference elevation): 41162425.945491925 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; ( R ) = ( 3.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.17e-07 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 19, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 14, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-04 ) ; ( Rwell ) = ( 6.19e-15 ) ; ( R ) = ( 2.27e-04 ) ; + Last LinSolve(iter,res) = ( 15, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.332177 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.056048 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.372e+07, 2.37604e+07, 2.38685e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.11426e+07, 1.12911e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 736.92 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 17.2018, 719.718 } rm^3 +compflowStatistics, reservoir: Phase mass: { 10148.8, 700886 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1488.72, 215343 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 8660.09, 485543 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 15.8039, 3.66487 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 10133, 700883 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 10148.8, 0 }, { 1784.78, 699058 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.34948e+07, 2.36545e+07, 2.37386e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.0917e+07, 1.11612e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.13 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.13 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219103 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65730.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153372 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219103 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27033e-08, 219103 } } kg +well_1Control: BHP (at the specified reference elevation): 41281777.165227 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 774.879 +compflowStatistics: Max component CFL number: 1064.7 +Time: 4.03612e+07s, dt:416538s, Cycle: 336 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; ( R ) = ( 3.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 22, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.34e-11 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 17, 8.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-04 ) ; ( Rwell ) = ( 4.26e-14 ) ; ( R ) = ( 1.51e-04 ) ; + Last LinSolve(iter,res) = ( 15, 9.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.381012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636344 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.07777e+07s, dt:222272s, Cycle: 337 +well_1Control: BHP (at the specified reference elevation): 41418771.239186786 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 1.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 11, 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 11, 8.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.202432 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0332781 +Time: 4.1e+07s, dt:222272s, Cycle: 338 +well_1Control: BHP (at the specified reference elevation): 41492113.12543758 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 1.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; ( R ) = ( 3.36e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 9.42e-09 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 2.91e-13 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 11, 9.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41565144.02572158 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.201944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0329241 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.39044e+07, 2.39449e+07, 2.40531e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.13568e+07, 1.15054e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.054 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 17.4796, 719.574 } rm^3 +compflowStatistics, reservoir: Phase mass: { 10372.7, 700848 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1519.63, 215414 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 8853.12, 485434 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 16.0472, 3.93911 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 10356.7, 700844 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 10372.7, 0 }, { 1815.43, 698989 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.36798e+07, 2.38391e+07, 2.3923e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.1132e+07, 1.13754e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.171 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.171 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219172 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65751.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153421 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219172 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27105e-08, 219172 } } kg +compflowStatistics: Max phase CFL number: 474.03 +compflowStatistics: Max component CFL number: 651.347 +Time: 4.12223e+07s, dt:343598s, Cycle: 339 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 2.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 8.24e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 18, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 13, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.67e-03 ) ; ( Rwell ) = ( 6.93e-13 ) ; ( R ) = ( 7.67e-03 ) ; + Last LinSolve(iter,res) = ( 13, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.99e-05 ) ; ( Rwell ) = ( 5.54e-16 ) ; ( R ) = ( 8.99e-05 ) ; + Last LinSolve(iter,res) = ( 15, 7.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.311038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0536977 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.15659e+07s, dt:406750s, Cycle: 340 +well_1Control: BHP (at the specified reference elevation): 41677090.308005005 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 1.92e-07 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 21, 9.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 16, 9.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.83e-05 ) ; ( Rwell ) = ( 2.51e-14 ) ; ( R ) = ( 4.83e-05 ) ; + Last LinSolve(iter,res) = ( 15, 8.25e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41809068.637586236 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.366175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061672 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.19726e+07s, dt:27380.8s, Cycle: 341 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 2.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.10e-10 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 8.47e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 7.47e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 6.49e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 5.74e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.84e-05 ) ; ( Rwell ) = ( 4.16e-14 ) ; ( R ) = ( 7.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00413696 +Time: 4.2e+07s, dt:27380.8s, Cycle: 342 +well_1Control: BHP (at the specified reference elevation): 41818065.89883838 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 2.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.98e-10 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 4.95e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.39e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.86e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.45e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.02e-05 ) ; ( Rwell ) = ( 4.00e-15 ) ; ( R ) = ( 4.02e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245741 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00411759 +well_1Control: BHP (at the specified reference elevation): 41827066.53484841 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.40758e+07, 2.41162e+07, 2.42245e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.15699e+07, 1.17186e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.178 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 17.7367, 719.442 } rm^3 +compflowStatistics, reservoir: Phase mass: { 10581, 700814 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1549.07, 215481 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 9031.98, 485333 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 16.6481, 4.21531 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 10564.4, 700810 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 10581, 0 }, { 1845.19, 698924 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.38521e+07, 2.40107e+07, 2.40944e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.13462e+07, 1.15885e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.21 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.21 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219237 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65771.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153466 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219237 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27173e-08, 219237 } } kg +compflowStatistics: Max phase CFL number: 58.0793 +compflowStatistics: Max component CFL number: 79.8066 +Time: 4.20274e+07s, dt:27380.8s, Cycle: 343 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 2.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.50e-03 ) ; ( Rwell ) = ( 1.94e-10 ) ; ( R ) = ( 7.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 1.10e-10 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 9.64e-11 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 8.47e-11 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 7.45e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 6.55e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 5.83e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.13e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.51e-11 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.97e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.81e-05 ) ; ( Rwell ) = ( 1.33e-14 ) ; ( R ) = ( 4.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245379 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00412786 +Time: 4.20548e+07s, dt:27380.8s, Cycle: 344 +well_1Control: BHP (at the specified reference elevation): 41836061.68153051 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 2.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 1.97e-10 ) ; ( R ) = ( 5.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 1.11e-10 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 9.82e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 8.64e-11 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 7.50e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 6.70e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 5.81e-11 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 5.19e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.57e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.02e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.53e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 2.54e-14 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00414972 +Time: 4.20821e+07s, dt:27380.8s, Cycle: 345 +well_1Control: BHP (at the specified reference elevation): 41845048.95688099 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 2.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 1.96e-10 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 8.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.10e-10 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.23e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.48e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.82e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.15e-05 ) ; ( Rwell ) = ( 1.74e-15 ) ; ( R ) = ( 5.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00415956 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.21095e+07s, dt:13690.4s, Cycle: 346 +well_1Control: BHP (at the specified reference elevation): 41854031.81868103 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 4.96e-11 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 3.82e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 9.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 9.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 9.40e-12 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.39e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.25e-06 ) ; ( Rwell ) = ( 2.01e-15 ) ; ( R ) = ( 3.25e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.58e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41858524.610899374 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.012282 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00207965 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.21232e+07s, dt:6845.2s, Cycle: 347 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 6.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-04 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00614837 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103997 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.21301e+07s, dt:13690.4s, Cycle: 348 +well_1Control: BHP (at the specified reference elevation): 41860768.90311098 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 4.99e-11 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 8.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 4.40e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 3.88e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 9.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 5.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 9.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.56e-05 ) ; ( Rwell ) = ( 6.52e-15 ) ; ( R ) = ( 3.56e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122822 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020797 +Time: 4.21437e+07s, dt:13690.4s, Cycle: 349 +well_1Control: BHP (at the specified reference elevation): 41865260.82882619 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 7.86e-12 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.04e-05 ) ; ( Rwell ) = ( 5.31e-15 ) ; ( R ) = ( 3.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122648 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00208058 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.21574e+07s, dt:6845.2s, Cycle: 350 +well_1Control: BHP (at the specified reference elevation): 41869752.848845854 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 6.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 8.01e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00615153 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104053 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.21643e+07s, dt:13690.4s, Cycle: 351 +well_1Control: BHP (at the specified reference elevation): 41871996.60524299 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 5.08e-11 ) ; ( R ) = ( 8.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 4.49e-11 ) ; ( R ) = ( 8.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 3.96e-11 ) ; ( R ) = ( 7.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 9.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 3.50e-11 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 9.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 6.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.85e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 5.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.45e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 5.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 7.16e-15 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41876487.6352654 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0122693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00208107 +Time: 4.2178e+07s, dt:13690.4s, Cycle: 352 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 4.85e-11 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 9.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 3.30e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.50e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.79e-05 ) ; ( Rwell ) = ( 1.19e-15 ) ; ( R ) = ( 1.79e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122518 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00208016 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.21917e+07s, dt:6845.2s, Cycle: 353 +well_1Control: BHP (at the specified reference elevation): 41880977.200021654 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 6.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.52e-04 ) ; ( Rwell ) = ( 8.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 8.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00613825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103955 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.21985e+07s, dt:13690.4s, Cycle: 354 +well_1Control: BHP (at the specified reference elevation): 41883215.35269739 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 4.90e-11 ) ; ( R ) = ( 6.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 4.31e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 9.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 9.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 9.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 2.94e-11 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.72e-05 ) ; ( Rwell ) = ( 7.32e-15 ) ; ( R ) = ( 1.72e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.34e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41887694.082831904 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0122541 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00207658 +Time: 4.22122e+07s, dt:13690.4s, Cycle: 355 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 4.97e-11 ) ; ( R ) = ( 6.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 3.82e-11 ) ; ( R ) = ( 6.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 5.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 5.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 2.62e-11 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 9.16e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 8.06e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 7.10e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 6.26e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.15e-05 ) ; ( Rwell ) = ( 4.64e-15 ) ; ( R ) = ( 1.15e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122497 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00207268 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.22259e+07s, dt:6845.2s, Cycle: 356 +well_1Control: BHP (at the specified reference elevation): 41892172.44725941 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 6.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 9.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41894408.77704947 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00613085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010352 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.22327e+07s, dt:13690.4s, Cycle: 357 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.40e-03 ) ; ( Rwell ) = ( 4.90e-11 ) ; ( R ) = ( 7.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 4.26e-11 ) ; ( R ) = ( 6.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 9.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 5.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 5.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 9.67e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 8.54e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.03e-05 ) ; ( Rwell ) = ( 1.11e-14 ) ; ( R ) = ( 4.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.09e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41898884.56376264 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0122557 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206492 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.22464e+07s, dt:6845.2s, Cycle: 358 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 6.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 8.79e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0061294 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103088 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.22533e+07s, dt:13690.4s, Cycle: 359 +well_1Control: BHP (at the specified reference elevation): 41901119.76290521 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 4.92e-11 ) ; ( R ) = ( 6.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 4.34e-11 ) ; ( R ) = ( 6.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 3.82e-11 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 5.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 2.72e-11 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 5.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.11e-05 ) ; ( Rwell ) = ( 9.49e-15 ) ; ( R ) = ( 4.11e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122502 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206133 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.2267e+07s, dt:6845.2s, Cycle: 360 +well_1Control: BHP (at the specified reference elevation): 41905594.2285648 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 5.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-04 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 9.28e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00612671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103157 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.22738e+07s, dt:13690.4s, Cycle: 361 +well_1Control: BHP (at the specified reference elevation): 41907825.94716264 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.87e-03 ) ; ( Rwell ) = ( 4.90e-11 ) ; ( R ) = ( 7.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.48e-03 ) ; ( Rwell ) = ( 4.31e-11 ) ; ( R ) = ( 7.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 3.81e-11 ) ; ( R ) = ( 7.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.93e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 6.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 6.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 5.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 9.55e-12 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.09e-05 ) ; ( Rwell ) = ( 9.36e-15 ) ; ( R ) = ( 4.09e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122604 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206485 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.22875e+07s, dt:6845.2s, Cycle: 362 +well_1Control: BHP (at the specified reference elevation): 41912301.66761634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 5.96e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-04 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.25e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.86e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 9.53e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41914538.367577955 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0061228 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103269 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.22943e+07s, dt:13690.4s, Cycle: 363 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 4.94e-11 ) ; ( R ) = ( 7.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 4.35e-11 ) ; ( R ) = ( 7.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 6.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 3.38e-11 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 2.98e-11 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 2.63e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.45e-03 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 5.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 4.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 9.69e-12 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 8.56e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.12e-05 ) ; ( Rwell ) = ( 5.63e-15 ) ; ( R ) = ( 4.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122474 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206526 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.2308e+07s, dt:6845.2s, Cycle: 364 +well_1Control: BHP (at the specified reference elevation): 41919011.0150723 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 5.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-04 ) ; ( Rwell ) = ( 7.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 9.80e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00612234 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103235 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.23149e+07s, dt:13690.4s, Cycle: 365 +well_1Control: BHP (at the specified reference elevation): 41921246.58824688 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 4.93e-11 ) ; ( R ) = ( 7.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 4.34e-11 ) ; ( R ) = ( 7.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 6.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 2.62e-11 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 4.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 9.69e-12 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.74e-05 ) ; ( Rwell ) = ( 8.48e-15 ) ; ( R ) = ( 3.74e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122456 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206446 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.23286e+07s, dt:6845.2s, Cycle: 366 +well_1Control: BHP (at the specified reference elevation): 41925717.78070685 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 5.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.43e-04 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 9.35e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00612161 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103294 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.23354e+07s, dt:13690.4s, Cycle: 367 +well_1Control: BHP (at the specified reference elevation): 41927951.59578439 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 4.91e-11 ) ; ( R ) = ( 5.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 4.32e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 3.81e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 2.69e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 9.49e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.17e-06 ) ; ( Rwell ) = ( 7.06e-15 ) ; ( R ) = ( 7.17e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122456 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206821 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.23491e+07s, dt:6845.2s, Cycle: 368 +well_1Control: BHP (at the specified reference elevation): 41932420.86290192 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 5.97e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 41934653.3961454 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00612092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103639 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.2356e+07s, dt:13690.4s, Cycle: 369 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 4.91e-11 ) ; ( R ) = ( 6.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 4.32e-11 ) ; ( R ) = ( 6.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.31e-03 ) ; ( Rwell ) = ( 3.81e-11 ) ; ( R ) = ( 6.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 5.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 2.59e-11 ) ; ( R ) = ( 5.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 2.28e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 9.51e-12 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.41e-06 ) ; ( Rwell ) = ( 6.33e-15 ) ; ( R ) = ( 7.41e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122446 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00208339 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.23696e+07s, dt:6845.2s, Cycle: 370 +well_1Control: BHP (at the specified reference elevation): 41939120.136854276 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 5.99e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-04 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.47e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00612009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104426 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.23765e+07s, dt:13690.4s, Cycle: 371 +well_1Control: BHP (at the specified reference elevation): 41941350.43764209 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; ( R ) = ( 7.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; ( R ) = ( 7.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 9.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; ( R ) = ( 6.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 9.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.33e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 6.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 2.93e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 1.91e-15 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020972 +Time: 4.23902e+07s, dt:13690.4s, Cycle: 372 +well_1Control: BHP (at the specified reference elevation): 41945818.2804942 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 5.03e-11 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.41e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 4.45e-11 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.38e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 9.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 3.77e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.39e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 6845.199288101867 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 6.02e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.52e-04 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.47e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611973 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010506 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 6845.199288101867, remaining dt = 6845.199288101867 +well_1Control: BHP (at the specified reference elevation): 41948046.840126336 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.26e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.88e-05 ) ; ( Rwell ) = ( 2.13e-15 ) ; ( R ) = ( 1.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00613864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105225 +Time: 4.24039e+07s, dt:6845.2s, Cycle: 373 +well_1Control: BHP (at the specified reference elevation): 41950281.40151778 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 6.05e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.29e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.66e-04 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.99e-12 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611942 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105406 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.24107e+07s, dt:13690.4s, Cycle: 374 +well_1Control: BHP (at the specified reference elevation): 41952509.84226057 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.86e-03 ) ; ( Rwell ) = ( 4.87e-11 ) ; ( R ) = ( 7.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 8.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 4.29e-11 ) ; ( R ) = ( 7.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 3.76e-11 ) ; ( R ) = ( 6.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 5.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 8.18e-15 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122408 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00211368 +Time: 4.24244e+07s, dt:13690.4s, Cycle: 375 +well_1Control: BHP (at the specified reference elevation): 41956974.83417764 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 4.81e-11 ) ; ( R ) = ( 6.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 6.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 4.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 9.04e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.50e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 7.71e-06 ) ; ( Rwell ) = ( 3.62e-15 ) ; ( R ) = ( 7.71e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122385 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00211812 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.24381e+07s, dt:6845.2s, Cycle: 376 +well_1Control: BHP (at the specified reference elevation): 41961430.93913307 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-04 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.28e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.49e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611906 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106 +Time: 4.24449e+07s, dt:6845.2s, Cycle: 377 +well_1Control: BHP (at the specified reference elevation): 41963656.01981823 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 9.49e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 9.78e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.71e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 8.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611665 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106074 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.24518e+07s, dt:13690.4s, Cycle: 378 +well_1Control: BHP (at the specified reference elevation): 41965882.19718621 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 5.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 4.18e-11 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 3.68e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.63e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.22e-12 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 2.07e-15 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122406 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00212313 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.24655e+07s, dt:6845.2s, Cycle: 379 +well_1Control: BHP (at the specified reference elevation): 41970333.95888032 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-04 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.94e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-04 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.61e-04 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611804 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106185 +Time: 4.24723e+07s, dt:6845.2s, Cycle: 380 +well_1Control: BHP (at the specified reference elevation): 41972558.29722491 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 9.49e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 9.04e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.02e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.05e-05 ) ; ( Rwell ) = ( 1.29e-15 ) ; ( R ) = ( 2.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00612945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106182 +Time: 4.24792e+07s, dt:6845.2s, Cycle: 381 +well_1Control: BHP (at the specified reference elevation): 41974785.38447519 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.34e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611733 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106189 +Time: 4.2486e+07s, dt:6845.2s, Cycle: 382 +well_1Control: BHP (at the specified reference elevation): 41977009.33766409 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 9.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.75e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.61e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.61e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 1.89e-15 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00612457 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106157 +Time: 4.24929e+07s, dt:6845.2s, Cycle: 383 +well_1Control: BHP (at the specified reference elevation): 41979235.69112204 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-04 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0061165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106165 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.24997e+07s, dt:13690.4s, Cycle: 384 +well_1Control: BHP (at the specified reference elevation): 41981458.54085274 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 4.92e-11 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 4.34e-11 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 3.82e-11 ) ; ( R ) = ( 6.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 5.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 5.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 2.28e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 2.24e-15 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.012237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00211974 +Time: 4.25134e+07s, dt:13690.4s, Cycle: 385 +well_1Control: BHP (at the specified reference elevation): 41985907.54781507 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 4.86e-11 ) ; ( R ) = ( 6.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 3.74e-11 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 3.29e-11 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 2.90e-11 ) ; ( R ) = ( 5.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 4.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 8.20e-12 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.36e-05 ) ; ( Rwell ) = ( 3.99e-16 ) ; ( R ) = ( 1.36e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122326 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00211496 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.25271e+07s, dt:6845.2s, Cycle: 386 +well_1Control: BHP (at the specified reference elevation): 41990357.86340324 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-04 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.32e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611563 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105661 +Time: 4.25339e+07s, dt:6845.2s, Cycle: 387 +well_1Control: BHP (at the specified reference elevation): 41992581.737959035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 9.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 9.41e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.29e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 2.16e-17 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611618 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105534 +Time: 4.25408e+07s, dt:6845.2s, Cycle: 388 +well_1Control: BHP (at the specified reference elevation): 41994806.889642715 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-04 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.84e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-04 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 9.35e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611428 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105445 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.25476e+07s, dt:13690.4s, Cycle: 389 +well_1Control: BHP (at the specified reference elevation): 41997028.384521 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 4.59e-11 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 4.01e-11 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 3.71e-11 ) ; ( R ) = ( 6.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.95e-05 ) ; ( Rwell ) = ( 1.77e-15 ) ; ( R ) = ( 1.95e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00210244 +Time: 4.25613e+07s, dt:13690.4s, Cycle: 390 +well_1Control: BHP (at the specified reference elevation): 42001476.21222653 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 6.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 3.70e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 3.26e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.28e-05 ) ; ( Rwell ) = ( 9.06e-15 ) ; ( R ) = ( 3.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00209584 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.2575e+07s, dt:6845.2s, Cycle: 391 +well_1Control: BHP (at the specified reference elevation): 42005923.62883933 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-04 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-04 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 4.22e-12 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104841 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.25818e+07s, dt:13690.4s, Cycle: 392 +well_1Control: BHP (at the specified reference elevation): 42008144.56078254 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 5.01e-11 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 4.43e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 3.92e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 3.46e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.18e-05 ) ; ( Rwell ) = ( 5.69e-15 ) ; ( R ) = ( 2.18e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42012590.46387981 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0122279 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00210008 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.25955e+07s, dt:6845.2s, Cycle: 393 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-04 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 9.47e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105042 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.26024e+07s, dt:13690.4s, Cycle: 394 +well_1Control: BHP (at the specified reference elevation): 42014808.35147856 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.34e-05 ) ; ( Rwell ) = ( 2.96e-13 ) ; ( R ) = ( 1.34e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122276 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00210204 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.26161e+07s, dt:6845.2s, Cycle: 395 +well_1Control: BHP (at the specified reference elevation): 42019253.56604187 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.35e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 9.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611115 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105192 +Time: 4.26229e+07s, dt:6845.2s, Cycle: 396 +well_1Control: BHP (at the specified reference elevation): 42021474.197380215 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 9.56e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.79e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 4.24e-15 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611236 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105271 +Time: 4.26298e+07s, dt:6845.2s, Cycle: 397 +well_1Control: BHP (at the specified reference elevation): 42023697.25387325 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-04 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.22e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00611055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105353 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.26366e+07s, dt:13690.4s, Cycle: 398 +well_1Control: BHP (at the specified reference elevation): 42025915.638940215 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 4.19e-11 ) ; ( R ) = ( 4.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.25e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 7.01e-12 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.72e-05 ) ; ( Rwell ) = ( 4.67e-15 ) ; ( R ) = ( 1.72e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00210849 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.26503e+07s, dt:6845.2s, Cycle: 399 +well_1Control: BHP (at the specified reference elevation): 42030361.50779694 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.35e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 9.98e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610954 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105458 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.26571e+07s, dt:13690.4s, Cycle: 400 +well_1Control: BHP (at the specified reference elevation): 42032579.99255194 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 4.74e-11 ) ; ( R ) = ( 7.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 4.13e-11 ) ; ( R ) = ( 6.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 5.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 3.18e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.31e-03 ) ; ( Rwell ) = ( 2.80e-11 ) ; ( R ) = ( 5.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 9.91e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 8.70e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.83e-05 ) ; ( Rwell ) = ( 5.79e-15 ) ; ( R ) = ( 3.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.01222 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00210891 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.26708e+07s, dt:6845.2s, Cycle: 401 +well_1Control: BHP (at the specified reference elevation): 42037018.49737032 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.69e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.83e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.05e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 9.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105431 +Time: 4.26777e+07s, dt:6845.2s, Cycle: 402 +well_1Control: BHP (at the specified reference elevation): 42039233.60232308 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.58e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.73e-05 ) ; ( Rwell ) = ( 6.69e-15 ) ; ( R ) = ( 1.73e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0061093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105381 +Time: 4.26845e+07s, dt:6845.2s, Cycle: 403 +well_1Control: BHP (at the specified reference elevation): 42041452.64220494 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.78e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.37e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.89e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 9.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105354 +Time: 4.26914e+07s, dt:6845.2s, Cycle: 404 +well_1Control: BHP (at the specified reference elevation): 42043665.22488897 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 9.64e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 8.59e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.50e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.65e-05 ) ; ( Rwell ) = ( 1.83e-16 ) ; ( R ) = ( 1.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0061092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105278 +Time: 4.26982e+07s, dt:6845.2s, Cycle: 405 +well_1Control: BHP (at the specified reference elevation): 42045885.4336948 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.34e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.37e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42048098.39503881 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00610726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105219 +Time: 4.27051e+07s, dt:6845.2s, Cycle: 406 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 9.41e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.90e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.26e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.28e-05 ) ; ( Rwell ) = ( 2.99e-15 ) ; ( R ) = ( 2.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105085 +Time: 4.27119e+07s, dt:6845.2s, Cycle: 407 +well_1Control: BHP (at the specified reference elevation): 42050319.00368634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.37e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.88e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.45e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 9.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42052532.93218693 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00610625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104952 +Time: 4.27187e+07s, dt:6845.2s, Cycle: 408 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.62e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 9.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.46e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.46e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.86e-05 ) ; ( Rwell ) = ( 2.41e-15 ) ; ( R ) = ( 1.86e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.001048 +Time: 4.27256e+07s, dt:6845.2s, Cycle: 409 +well_1Control: BHP (at the specified reference elevation): 42054752.35275832 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.28e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 9.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104676 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.27324e+07s, dt:13690.4s, Cycle: 410 +well_1Control: BHP (at the specified reference elevation): 42056968.20054827 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 4.19e-11 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 9.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 6.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 8.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 6.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.31e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 5.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.09e-05 ) ; ( Rwell ) = ( 4.26e-15 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122114 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00208685 +Time: 4.27461e+07s, dt:13690.4s, Cycle: 411 +well_1Control: BHP (at the specified reference elevation): 42061402.50148736 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.77e-03 ) ; ( Rwell ) = ( 4.71e-11 ) ; ( R ) = ( 6.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 3.64e-11 ) ; ( R ) = ( 6.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 8.11e-12 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.50e-05 ) ; ( Rwell ) = ( 5.34e-15 ) ; ( R ) = ( 3.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42065835.26077258 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0122084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00208853 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.27598e+07s, dt:6845.2s, Cycle: 412 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 7.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104586 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.27667e+07s, dt:13690.4s, Cycle: 413 +well_1Control: BHP (at the specified reference elevation): 42068049.86853528 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 4.81e-11 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 4.18e-11 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 3.71e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 3.23e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 9.04e-12 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.37e-05 ) ; ( Rwell ) = ( 2.07e-15 ) ; ( R ) = ( 1.37e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00209534 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.27804e+07s, dt:6845.2s, Cycle: 414 +well_1Control: BHP (at the specified reference elevation): 42072479.81893021 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-04 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 9.07e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610143 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00104874 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.27872e+07s, dt:13690.4s, Cycle: 415 +well_1Control: BHP (at the specified reference elevation): 42074693.30675213 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.23e-03 ) ; ( Rwell ) = ( 4.68e-11 ) ; ( R ) = ( 6.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 4.11e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 3.63e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 3.19e-11 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 9.36e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.84e-05 ) ; ( Rwell ) = ( 9.70e-15 ) ; ( R ) = ( 3.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42079121.49377158 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0122062 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00209948 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.28009e+07s, dt:6845.2s, Cycle: 416 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 7.19e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00610014 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105029 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.28077e+07s, dt:13690.4s, Cycle: 417 +well_1Control: BHP (at the specified reference elevation): 42081333.292327724 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.88e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 4.29e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 9.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 8.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 9.77e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.51e-05 ) ; ( Rwell ) = ( 5.25e-15 ) ; ( R ) = ( 1.51e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0021059 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.28214e+07s, dt:6845.2s, Cycle: 418 +well_1Control: BHP (at the specified reference elevation): 42085759.76171458 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-04 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.52e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.74e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 9.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105599 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.28283e+07s, dt:13690.4s, Cycle: 419 +well_1Control: BHP (at the specified reference elevation): 42087970.10193499 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.59e-03 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 6.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.33e-03 ) ; ( Rwell ) = ( 4.19e-11 ) ; ( R ) = ( 6.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 3.68e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 8.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 3.25e-11 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.48e-06 ) ; ( Rwell ) = ( 1.28e-14 ) ; ( R ) = ( 8.48e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00212229 +Time: 4.2842e+07s, dt:13690.4s, Cycle: 420 +well_1Control: BHP (at the specified reference elevation): 42092395.82974503 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; ( R ) = ( 6.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; ( R ) = ( 5.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 9.01e-12 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 7.95e-12 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.97e-05 ) ; ( Rwell ) = ( 4.93e-15 ) ; ( R ) = ( 2.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121957 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00213174 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.28556e+07s, dt:6845.2s, Cycle: 421 +well_1Control: BHP (at the specified reference elevation): 42096821.227775455 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.72e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.006097 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010681 +Time: 4.28625e+07s, dt:6845.2s, Cycle: 422 +well_1Control: BHP (at the specified reference elevation): 42099031.64572349 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.13e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.51e-05 ) ; ( Rwell ) = ( 8.44e-16 ) ; ( R ) = ( 2.51e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060979 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107009 +Time: 4.28693e+07s, dt:6845.2s, Cycle: 423 +well_1Control: BHP (at the specified reference elevation): 42101244.0061167 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.75e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 7.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 9.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42103453.77727203 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00609563 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107222 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.28762e+07s, dt:13690.4s, Cycle: 424 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 4.62e-11 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 4.07e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 3.57e-11 ) ; ( R ) = ( 5.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 8.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 9.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 9.88e-12 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.54e-05 ) ; ( Rwell ) = ( 3.06e-15 ) ; ( R ) = ( 1.54e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121926 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00214999 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.28899e+07s, dt:6845.2s, Cycle: 425 +well_1Control: BHP (at the specified reference elevation): 42107878.74956733 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.40e-11 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.41e-11 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 7.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.05e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 9.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00609437 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107567 +Time: 4.28967e+07s, dt:6845.2s, Cycle: 426 +well_1Control: BHP (at the specified reference elevation): 42110087.737897225 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 9.53e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.35e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.25e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 2.96e-16 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00609516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107615 +Time: 4.29036e+07s, dt:6845.2s, Cycle: 427 +well_1Control: BHP (at the specified reference elevation): 42112297.68006182 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-04 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 9.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00609298 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107756 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.29104e+07s, dt:13690.4s, Cycle: 428 +well_1Control: BHP (at the specified reference elevation): 42114504.38523435 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 4.64e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 4.08e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 9.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 8.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.44e-06 ) ; ( Rwell ) = ( 3.43e-15 ) ; ( R ) = ( 7.44e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121885 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00215793 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.29241e+07s, dt:6845.2s, Cycle: 429 +well_1Control: BHP (at the specified reference elevation): 42118922.62916483 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 8.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.90e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.61e-04 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-04 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 7.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00609155 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107993 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.29309e+07s, dt:13690.4s, Cycle: 430 +well_1Control: BHP (at the specified reference elevation): 42121127.94050416 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 4.64e-11 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 4.08e-11 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 3.25e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 5.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 8.11e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.65e-05 ) ; ( Rwell ) = ( 7.30e-15 ) ; ( R ) = ( 3.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121878 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00216103 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.29446e+07s, dt:6845.2s, Cycle: 431 +well_1Control: BHP (at the specified reference elevation): 42125544.423609324 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-04 ) ; ( Rwell ) = ( 8.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.00e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.006091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108121 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.29515e+07s, dt:13690.4s, Cycle: 432 +well_1Control: BHP (at the specified reference elevation): 42127749.833719745 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 4.67e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 4.11e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 3.18e-11 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 2.80e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 8.73e-12 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.19e-05 ) ; ( Rwell ) = ( 5.36e-15 ) ; ( R ) = ( 3.19e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121833 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00216561 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.29652e+07s, dt:6845.2s, Cycle: 433 +well_1Control: BHP (at the specified reference elevation): 42132166.56903154 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 6.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 8.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.41e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-04 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 9.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00608897 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108353 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.2972e+07s, dt:13690.4s, Cycle: 434 +well_1Control: BHP (at the specified reference elevation): 42134372.43259457 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 4.66e-11 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 4.10e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 3.60e-11 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 3.17e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 2.78e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 2.45e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 8.96e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.76e-05 ) ; ( Rwell ) = ( 6.53e-15 ) ; ( R ) = ( 3.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42138787.45524831 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0121805 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00217158 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.29857e+07s, dt:6845.2s, Cycle: 435 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 7.00e-12 ) ; ( R ) = ( 9.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00608689 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00109105 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.29926e+07s, dt:7446.1s, Cycle: 436 +well_1Control: BHP (at the specified reference elevation): 42140992.27944584 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 9.26e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.23e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.22e-05 ) ; ( Rwell ) = ( 3.40e-15 ) ; ( R ) = ( 1.22e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00662558 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.001187 +Time: 4.3e+07s, dt:7446.1s, Cycle: 437 +well_1Control: BHP (at the specified reference elevation): 42143392.98180409 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.90e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 9.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00662003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118689 +well_1Control: BHP (at the specified reference elevation): 42145791.66037069 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.42855e+07, 2.43259e+07, 2.44343e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.17839e+07, 1.19327e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.331 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 18.0554, 719.275 } rm^3 +compflowStatistics, reservoir: Phase mass: { 10839.5, 700767 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1583.26, 215562 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 9256.24, 485205 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 16.8489, 4.7656 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 10822.6, 700762 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 10839.5, 0 }, { 1876.51, 698844 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.40617e+07, 2.42205e+07, 2.43041e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.15602e+07, 1.18025e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.256 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.256 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219316 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65794.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153521 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219316 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27255e-08, 219316 } } kg +compflowStatistics: Max phase CFL number: 15.6926 +compflowStatistics: Max component CFL number: 21.5638 +Time: 4.30074e+07s, dt:7446.1s, Cycle: 438 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.90e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 9.32e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 7.03e-15 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00662221 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118656 +Time: 4.30149e+07s, dt:7446.1s, Cycle: 439 +well_1Control: BHP (at the specified reference elevation): 42148193.70019624 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 8.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.75e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-04 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.77e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 7.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.90e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 9.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0066189 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118639 +Time: 4.30223e+07s, dt:7446.1s, Cycle: 440 +well_1Control: BHP (at the specified reference elevation): 42150593.19555448 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.47e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 9.82e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.44e-06 ) ; ( Rwell ) = ( 2.53e-15 ) ; ( R ) = ( 4.44e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0066202 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118603 +Time: 4.30298e+07s, dt:7446.1s, Cycle: 441 +well_1Control: BHP (at the specified reference elevation): 42152995.062261865 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.34e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 1.97e-12 ) ; ( R ) = ( 7.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42155394.20207417 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00661732 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118538 +Time: 4.30372e+07s, dt:7446.1s, Cycle: 442 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.42e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.13e-05 ) ; ( Rwell ) = ( 1.22e-15 ) ; ( R ) = ( 1.13e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661927 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118432 +Time: 4.30447e+07s, dt:7446.1s, Cycle: 443 +well_1Control: BHP (at the specified reference elevation): 42157795.82869568 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.27e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-04 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.68e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.74e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42160194.43464683 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00661562 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118319 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.30521e+07s, dt:14892.2s, Cycle: 444 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.91e-03 ) ; ( Rwell ) = ( 5.65e-11 ) ; ( R ) = ( 7.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 4.87e-11 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 4.28e-11 ) ; ( R ) = ( 6.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 3.77e-11 ) ; ( R ) = ( 6.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 5.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 5.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 5.59e-15 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.013235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00236114 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.3067e+07s, dt:7446.1s, Cycle: 445 +well_1Control: BHP (at the specified reference elevation): 42164996.75884947 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 8.38e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.52e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 2.64e-12 ) ; ( R ) = ( 9.67e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661411 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00117904 +Time: 4.30745e+07s, dt:7446.1s, Cycle: 446 +well_1Control: BHP (at the specified reference elevation): 42167395.23295988 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.38e-10 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.37e-10 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.40e-10 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.39e-10 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.38e-10 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.38e-10 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.34e-10 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.34e-10 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.31e-10 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.31e-10 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.31e-10 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.23e-05 ) ; ( Rwell ) = ( 2.01e-13 ) ; ( R ) = ( 1.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661608 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118069 +Time: 4.30819e+07s, dt:7446.1s, Cycle: 447 +well_1Control: BHP (at the specified reference elevation): 42169797.30872625 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.34e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.39e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661278 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00117916 +Time: 4.30894e+07s, dt:7446.1s, Cycle: 448 +well_1Control: BHP (at the specified reference elevation): 42172195.698275834 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.71e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.71e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.57e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.56e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.68e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.91e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.43e-05 ) ; ( Rwell ) = ( 1.33e-16 ) ; ( R ) = ( 2.43e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118 +Time: 4.30968e+07s, dt:7446.1s, Cycle: 449 +well_1Control: BHP (at the specified reference elevation): 42174596.7760221 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.41e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.85e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118321 +Time: 4.31042e+07s, dt:7446.1s, Cycle: 450 +well_1Control: BHP (at the specified reference elevation): 42176993.26434818 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.50e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.98e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.92e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 7.85e-16 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0066141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.001186 +Time: 4.31117e+07s, dt:7446.1s, Cycle: 451 +well_1Control: BHP (at the specified reference elevation): 42179393.907463446 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.20e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.07e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660973 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118885 +Time: 4.31191e+07s, dt:7446.1s, Cycle: 452 +well_1Control: BHP (at the specified reference elevation): 42181789.881318495 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.72e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.21e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-05 ) ; ( Rwell ) = ( 8.54e-15 ) ; ( R ) = ( 1.34e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119142 +Time: 4.31266e+07s, dt:7446.1s, Cycle: 453 +well_1Control: BHP (at the specified reference elevation): 42184190.04693228 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.86e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.63e-11 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.34e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.39e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42186582.68704569 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00660827 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119384 +Time: 4.3134e+07s, dt:7446.1s, Cycle: 454 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.67e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.52e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.48e-05 ) ; ( Rwell ) = ( 2.65e-15 ) ; ( R ) = ( 1.48e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661196 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119585 +Time: 4.31415e+07s, dt:7446.1s, Cycle: 455 +well_1Control: BHP (at the specified reference elevation): 42188979.43494989 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 8.05e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.35e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 9.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660743 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119788 +Time: 4.31489e+07s, dt:7446.1s, Cycle: 456 +well_1Control: BHP (at the specified reference elevation): 42191373.84052826 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.62e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.03e-05 ) ; ( Rwell ) = ( 2.65e-15 ) ; ( R ) = ( 2.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660929 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119928 +Time: 4.31564e+07s, dt:7446.1s, Cycle: 457 +well_1Control: BHP (at the specified reference elevation): 42193770.070139915 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.65e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.76e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 9.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660633 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012008 +Time: 4.31638e+07s, dt:7446.1s, Cycle: 458 +well_1Control: BHP (at the specified reference elevation): 42196164.61255361 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 9.14e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 1.02e-15 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660756 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120188 +Time: 4.31713e+07s, dt:7446.1s, Cycle: 459 +well_1Control: BHP (at the specified reference elevation): 42198560.539915085 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 8.62e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.64e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.74e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.22e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.73e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120295 +Time: 4.31787e+07s, dt:7446.1s, Cycle: 460 +well_1Control: BHP (at the specified reference elevation): 42200953.85932912 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.70e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.82e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 3.97e-15 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660645 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012036 +Time: 4.31862e+07s, dt:7446.1s, Cycle: 461 +well_1Control: BHP (at the specified reference elevation): 42203349.2158462 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.96e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 9.66e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120414 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.31936e+07s, dt:14892.2s, Cycle: 462 +well_1Control: BHP (at the specified reference elevation): 42205741.86336656 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.11e-03 ) ; ( Rwell ) = ( 5.53e-11 ) ; ( R ) = ( 7.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 4.86e-11 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 9.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 4.29e-11 ) ; ( R ) = ( 6.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 6.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 5.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 9.36e-12 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 3.91e-15 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0132094 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00241572 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.32085e+07s, dt:7446.1s, Cycle: 463 +well_1Control: BHP (at the specified reference elevation): 42210531.76823366 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.66e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121044 +Time: 4.32159e+07s, dt:7446.1s, Cycle: 464 +well_1Control: BHP (at the specified reference elevation): 42212925.37784567 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.67e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 9.96e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.81e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 9.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121297 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.32234e+07s, dt:14892.2s, Cycle: 465 +well_1Control: BHP (at the specified reference elevation): 42215319.431966215 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 5.58e-11 ) ; ( R ) = ( 7.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 4.91e-11 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 9.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 4.32e-11 ) ; ( R ) = ( 6.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 3.81e-11 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.23e-06 ) ; ( Rwell ) = ( 2.65e-15 ) ; ( R ) = ( 7.23e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0132023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243477 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.32383e+07s, dt:7446.1s, Cycle: 466 +well_1Control: BHP (at the specified reference elevation): 42220110.663432136 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659898 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121919 +Time: 4.32457e+07s, dt:7446.1s, Cycle: 467 +well_1Control: BHP (at the specified reference elevation): 42222504.43101232 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.78e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 9.20e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.39e-05 ) ; ( Rwell ) = ( 2.86e-15 ) ; ( R ) = ( 1.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122017 +Time: 4.32532e+07s, dt:7446.1s, Cycle: 468 +well_1Control: BHP (at the specified reference elevation): 42224900.5868385 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 9.49e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659716 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122132 +Time: 4.32606e+07s, dt:7446.1s, Cycle: 469 +well_1Control: BHP (at the specified reference elevation): 42227295.06257733 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.46e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 9.93e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.79e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.77e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.22e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 2.09e-15 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122254 +Time: 4.32681e+07s, dt:7446.1s, Cycle: 470 +well_1Control: BHP (at the specified reference elevation): 42229691.57037689 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.57e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 9.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42232087.21607885 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00659625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122364 +Time: 4.32755e+07s, dt:7446.1s, Cycle: 471 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.10e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.18e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.38e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.79e-05 ) ; ( Rwell ) = ( 2.79e-15 ) ; ( R ) = ( 1.79e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659683 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122446 +Time: 4.3283e+07s, dt:7446.1s, Cycle: 472 +well_1Control: BHP (at the specified reference elevation): 42234484.511691585 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 9.89e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659439 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122521 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.32904e+07s, dt:14892.2s, Cycle: 473 +well_1Control: BHP (at the specified reference elevation): 42236877.22311054 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 1.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 5.62e-11 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.03e-03 ) ; ( Rwell ) = ( 4.83e-11 ) ; ( R ) = ( 7.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 9.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 9.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 4.26e-11 ) ; ( R ) = ( 6.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 9.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 6.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 9.28e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.08e-05 ) ; ( Rwell ) = ( 6.24e-15 ) ; ( R ) = ( 1.08e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0131921 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245154 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.33053e+07s, dt:7446.1s, Cycle: 474 +well_1Control: BHP (at the specified reference elevation): 42241669.1849127 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.60e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659215 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122591 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.33127e+07s, dt:14892.2s, Cycle: 475 +well_1Control: BHP (at the specified reference elevation): 42244061.254976906 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; ( R ) = ( 6.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 9.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; ( R ) = ( 6.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 9.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; ( R ) = ( 5.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 9.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 7.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 8.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 2.90e-11 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.27e-05 ) ; ( Rwell ) = ( 3.63e-15 ) ; ( R ) = ( 1.27e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42248853.99426691 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0131872 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245035 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.33276e+07s, dt:7446.1s, Cycle: 476 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.10e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 9.07e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42251248.59856115 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00659059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122457 +Time: 4.33351e+07s, dt:7446.1s, Cycle: 477 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.71e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 8.77e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658857 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122392 +Time: 4.33425e+07s, dt:7446.1s, Cycle: 478 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 42253642.48522166 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 8.74e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 9.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.86e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.97e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 4.73e-16 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00659204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122287 +Time: 4.335e+07s, dt:7446.1s, Cycle: 479 +well_1Control: BHP (at the specified reference elevation): 42256040.30939397 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 8.44e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 9.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42258435.170992285 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00658863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012219 +Time: 4.33574e+07s, dt:7446.1s, Cycle: 480 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 9.57e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.80e-05 ) ; ( Rwell ) = ( 7.76e-15 ) ; ( R ) = ( 1.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122044 +Time: 4.33649e+07s, dt:7446.1s, Cycle: 481 +well_1Control: BHP (at the specified reference elevation): 42260831.80199362 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 7.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.67e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.06e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.70e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.54e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 3.94e-17 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121902 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.33723e+07s, dt:3723.05s, Cycle: 482 +well_1Control: BHP (at the specified reference elevation): 42263225.7756336 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 3.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-04 ) ; ( Rwell ) = ( 9.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-04 ) ; ( Rwell ) = ( 9.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-04 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.45e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.47e-04 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.30e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.16e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.47e-04 ) ; ( Rwell ) = ( 1.53e-12 ) ; ( R ) = ( 3.47e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.92e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42264422.282103136 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00329389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000609071 +Time: 4.3376e+07s, dt:3723.05s, Cycle: 483 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 3.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 9.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-04 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 9.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 9.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 8.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-04 ) ; ( Rwell ) = ( 9.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.02e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00331835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000608732 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.33798e+07s, dt:7446.1s, Cycle: 484 +well_1Control: BHP (at the specified reference elevation): 42265617.9465285 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.96e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.11e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.38e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42268008.75457214 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00658643 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121578 +Time: 4.33872e+07s, dt:7446.1s, Cycle: 485 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.70e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 9.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 9.41e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 6.23e-15 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658682 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121377 +Time: 4.33946e+07s, dt:7446.1s, Cycle: 486 +well_1Control: BHP (at the specified reference elevation): 42270402.28295887 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42272792.66028045 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00658465 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121182 +Time: 4.34021e+07s, dt:7446.1s, Cycle: 487 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 9.82e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.04e-05 ) ; ( Rwell ) = ( 5.78e-15 ) ; ( R ) = ( 2.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658656 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120994 +Time: 4.34095e+07s, dt:7446.1s, Cycle: 488 +well_1Control: BHP (at the specified reference elevation): 42275184.75894234 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.12e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 9.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658333 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121057 +Time: 4.3417e+07s, dt:7446.1s, Cycle: 489 +well_1Control: BHP (at the specified reference elevation): 42277573.6520223 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.80e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 9.71e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 7.62e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.43e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.09e-05 ) ; ( Rwell ) = ( 2.83e-15 ) ; ( R ) = ( 2.09e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121093 +Time: 4.34244e+07s, dt:7446.1s, Cycle: 490 +well_1Control: BHP (at the specified reference elevation): 42279966.554849096 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 9.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 9.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 8.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 9.28e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.12e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.66e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 7.05e-16 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121256 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.34319e+07s, dt:3723.05s, Cycle: 491 +well_1Control: BHP (at the specified reference elevation): 42282359.01182566 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 3.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 6.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00329197 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000606979 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.34356e+07s, dt:7446.1s, Cycle: 492 +well_1Control: BHP (at the specified reference elevation): 42283552.97313857 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 9.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00658169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121632 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.3443e+07s, dt:14892.2s, Cycle: 493 +well_1Control: BHP (at the specified reference elevation): 42285941.62662974 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 1.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.51e-03 ) ; ( Rwell ) = ( 5.51e-11 ) ; ( R ) = ( 7.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 9.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 4.85e-11 ) ; ( R ) = ( 7.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 9.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 4.27e-11 ) ; ( R ) = ( 6.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 3.76e-11 ) ; ( R ) = ( 6.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 6.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.23e-05 ) ; ( Rwell ) = ( 8.45e-15 ) ; ( R ) = ( 4.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0131628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.34579e+07s, dt:7446.1s, Cycle: 494 +well_1Control: BHP (at the specified reference elevation): 42290722.32909553 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 9.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 9.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.86e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.72e-05 ) ; ( Rwell ) = ( 2.50e-15 ) ; ( R ) = ( 1.72e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122156 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.34654e+07s, dt:3723.05s, Cycle: 495 +well_1Control: BHP (at the specified reference elevation): 42293113.47322635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.53e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 3.53e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 5.77e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42294307.09374601 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00329031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000611245 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.34691e+07s, dt:7446.1s, Cycle: 496 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 1.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-05 ) ; ( Rwell ) = ( 5.47e-16 ) ; ( R ) = ( 1.58e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657999 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122186 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.34766e+07s, dt:14892.2s, Cycle: 497 +well_1Control: BHP (at the specified reference elevation): 42296697.9863694 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 1.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 5.54e-11 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 6.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 5.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 5.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 4.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 9.26e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 8.33e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 1.08e-14 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0131551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244838 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.34914e+07s, dt:7446.1s, Cycle: 498 +well_1Control: BHP (at the specified reference elevation): 42301480.02666147 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.61e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.63e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.63e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.10e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 9.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122509 +Time: 4.34989e+07s, dt:7446.1s, Cycle: 499 +well_1Control: BHP (at the specified reference elevation): 42303869.50921111 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 9.48e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 8.46e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.37e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.23e-05 ) ; ( Rwell ) = ( 6.05e-15 ) ; ( R ) = ( 2.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122566 +Time: 4.35063e+07s, dt:7446.1s, Cycle: 500 +well_1Control: BHP (at the specified reference elevation): 42306260.59375624 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 9.53e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122625 +Time: 4.35138e+07s, dt:7446.1s, Cycle: 501 +well_1Control: BHP (at the specified reference elevation): 42308648.77688243 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.50e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 9.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.59e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.46e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.15e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.67e-06 ) ; ( Rwell ) = ( 4.92e-16 ) ; ( R ) = ( 5.67e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657622 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012262 +Time: 4.35212e+07s, dt:7446.1s, Cycle: 502 +well_1Control: BHP (at the specified reference elevation): 42311040.12893845 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.95e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 9.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657343 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122611 +Time: 4.35287e+07s, dt:7446.1s, Cycle: 503 +well_1Control: BHP (at the specified reference elevation): 42313429.77136311 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 9.77e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.86e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.81e-05 ) ; ( Rwell ) = ( 4.33e-16 ) ; ( R ) = ( 1.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.51e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42315821.34187932 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00657398 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122591 +Time: 4.35361e+07s, dt:7446.1s, Cycle: 504 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.46e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.86e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657219 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122578 +Time: 4.35436e+07s, dt:7446.1s, Cycle: 505 +well_1Control: BHP (at the specified reference elevation): 42318210.657174885 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 9.83e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.59e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 4.47e-15 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122501 +Time: 4.3551e+07s, dt:7446.1s, Cycle: 506 +well_1Control: BHP (at the specified reference elevation): 42320601.515170634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-04 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.51e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.34e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 9.90e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42322989.67172838 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.006571 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122419 +Time: 4.35585e+07s, dt:7446.1s, Cycle: 507 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 8.85e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.95e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.32e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.32e-05 ) ; ( Rwell ) = ( 1.92e-16 ) ; ( R ) = ( 2.32e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122319 +Time: 4.35659e+07s, dt:7446.1s, Cycle: 508 +well_1Control: BHP (at the specified reference elevation): 42325380.75362701 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.29e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656966 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122205 +Time: 4.35733e+07s, dt:7446.1s, Cycle: 509 +well_1Control: BHP (at the specified reference elevation): 42327769.81120336 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.52e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 9.07e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.93e-05 ) ; ( Rwell ) = ( 1.81e-15 ) ; ( R ) = ( 1.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00657008 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122065 +Time: 4.35808e+07s, dt:7446.1s, Cycle: 510 +well_1Control: BHP (at the specified reference elevation): 42330159.5608308 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 9.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 9.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 8.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 9.24e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 9.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656846 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012191 +Time: 4.35882e+07s, dt:7446.1s, Cycle: 511 +well_1Control: BHP (at the specified reference elevation): 42332547.45466936 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 9.56e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 9.07e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 8.05e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.10e-05 ) ; ( Rwell ) = ( 6.89e-17 ) ; ( R ) = ( 1.10e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.52e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42334937.22989555 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00656844 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121738 +Time: 4.35957e+07s, dt:7446.1s, Cycle: 512 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 7.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 8.54e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.57e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.72e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.73e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.67e-05 ) ; ( Rwell ) = ( 3.16e-15 ) ; ( R ) = ( 1.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.35e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42337324.493757345 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00656725 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121551 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.36031e+07s, dt:3723.05s, Cycle: 513 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 5.90e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00328421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000607313 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.36069e+07s, dt:7446.1s, Cycle: 514 +well_1Control: BHP (at the specified reference elevation): 42338516.85466993 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 9.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656812 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121239 +Time: 4.36143e+07s, dt:7446.1s, Cycle: 515 +well_1Control: BHP (at the specified reference elevation): 42340899.22391105 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.58e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 9.26e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 8.22e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.48e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.56e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.93e-05 ) ; ( Rwell ) = ( 2.08e-15 ) ; ( R ) = ( 1.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065665 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121013 +Time: 4.36217e+07s, dt:7446.1s, Cycle: 516 +well_1Control: BHP (at the specified reference elevation): 42343285.72474158 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 7.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 8.76e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 7.78e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.58e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.31e-05 ) ; ( Rwell ) = ( 2.43e-15 ) ; ( R ) = ( 1.31e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120759 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.36292e+07s, dt:3723.05s, Cycle: 517 +well_1Control: BHP (at the specified reference elevation): 42345672.239513114 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.53e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.53e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 6.21e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42346862.29078567 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00328329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000603163 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.36329e+07s, dt:7446.1s, Cycle: 518 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 2.18e-15 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656744 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120432 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.36404e+07s, dt:14892.2s, Cycle: 519 +well_1Control: BHP (at the specified reference elevation): 42349248.371266946 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 5.53e-11 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 3.75e-11 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.21e-06 ) ; ( Rwell ) = ( 4.03e-15 ) ; ( R ) = ( 8.21e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0131269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240873 +Time: 4.36553e+07s, dt:14892.2s, Cycle: 520 +well_1Control: BHP (at the specified reference elevation): 42354018.59718214 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 5.45e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 9.78e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 8.62e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 7.60e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.57e-05 ) ; ( Rwell ) = ( 9.05e-16 ) ; ( R ) = ( 1.57e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0131245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240739 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.36701e+07s, dt:7446.1s, Cycle: 521 +well_1Control: BHP (at the specified reference elevation): 42358788.95179357 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 7.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.47e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 9.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656064 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120323 +Time: 4.36776e+07s, dt:7446.1s, Cycle: 522 +well_1Control: BHP (at the specified reference elevation): 42361171.74055141 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 8.96e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.94e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 5.51e-15 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065624 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120206 +Time: 4.3685e+07s, dt:7446.1s, Cycle: 523 +well_1Control: BHP (at the specified reference elevation): 42363556.4796678 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 7.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.68e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.87e-12 ) ; ( R ) = ( 9.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00655939 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120102 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.36925e+07s, dt:3723.05s, Cycle: 524 +well_1Control: BHP (at the specified reference elevation): 42365939.47837533 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 4.81e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0032935 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000600212 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.36962e+07s, dt:7446.1s, Cycle: 525 +well_1Control: BHP (at the specified reference elevation): 42367130.384621784 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.64e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.51e-05 ) ; ( Rwell ) = ( 3.94e-16 ) ; ( R ) = ( 1.51e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119883 +Time: 4.37037e+07s, dt:7446.1s, Cycle: 526 +well_1Control: BHP (at the specified reference elevation): 42369513.39289053 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.99e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.60e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.64e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 9.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42371895.94075997 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00655752 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119754 +Time: 4.37111e+07s, dt:7446.1s, Cycle: 527 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.62e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.04e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.93e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.71e-05 ) ; ( Rwell ) = ( 4.28e-15 ) ; ( R ) = ( 1.71e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00655949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119562 +Time: 4.37185e+07s, dt:7446.1s, Cycle: 528 +well_1Control: BHP (at the specified reference elevation): 42374280.812547356 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 9.79e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00655641 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119378 +Time: 4.3726e+07s, dt:7446.1s, Cycle: 529 +well_1Control: BHP (at the specified reference elevation): 42376664.78110563 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 8.14e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.81e-05 ) ; ( Rwell ) = ( 2.07e-15 ) ; ( R ) = ( 1.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065572 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119156 +Time: 4.37334e+07s, dt:7446.1s, Cycle: 530 +well_1Control: BHP (at the specified reference elevation): 42379049.56477066 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.97e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.52e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.89e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 9.62e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00655496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119082 +Time: 4.37409e+07s, dt:7446.1s, Cycle: 531 +well_1Control: BHP (at the specified reference elevation): 42381433.5875393 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.60e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.89e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.63e-05 ) ; ( Rwell ) = ( 8.01e-15 ) ; ( R ) = ( 1.63e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42383818.60710366 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00655546 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119021 +Time: 4.37483e+07s, dt:7446.1s, Cycle: 532 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.52e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00655357 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119062 +Time: 4.37558e+07s, dt:7446.1s, Cycle: 533 +well_1Control: BHP (at the specified reference elevation): 42386202.703742534 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.98e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.97e-06 ) ; ( Rwell ) = ( 2.70e-16 ) ; ( R ) = ( 7.97e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.22e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42388588.05449627 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00655444 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118984 +Time: 4.37632e+07s, dt:7446.1s, Cycle: 534 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 9.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00655233 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119071 +Time: 4.37707e+07s, dt:7446.1s, Cycle: 535 +well_1Control: BHP (at the specified reference elevation): 42390972.46550704 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.81e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 9.40e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.93e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 3.72e-15 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42393358.37427893 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00655325 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119121 +Time: 4.37781e+07s, dt:7446.1s, Cycle: 536 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.26e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 9.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119195 +Time: 4.37856e+07s, dt:7446.1s, Cycle: 537 +well_1Control: BHP (at the specified reference elevation): 42395742.75909941 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.68e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 8.70e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.83e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.06e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.37e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.22e-05 ) ; ( Rwell ) = ( 3.41e-15 ) ; ( R ) = ( 1.22e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119215 +Time: 4.3793e+07s, dt:7446.1s, Cycle: 538 +well_1Control: BHP (at the specified reference elevation): 42398127.50940205 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.09e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 3.58e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654924 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0011924 +Time: 4.38005e+07s, dt:7446.1s, Cycle: 539 +well_1Control: BHP (at the specified reference elevation): 42400510.989955485 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.50e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 8.56e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.57e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.11e-05 ) ; ( Rwell ) = ( 1.73e-15 ) ; ( R ) = ( 1.11e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0065515 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119217 +Time: 4.38079e+07s, dt:7446.1s, Cycle: 540 +well_1Control: BHP (at the specified reference elevation): 42402895.06224842 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 8.16e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.54e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 9.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654771 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119204 +Time: 4.38153e+07s, dt:7446.1s, Cycle: 541 +well_1Control: BHP (at the specified reference elevation): 42405277.19560823 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.84e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.40e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.73e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.84e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.12e-06 ) ; ( Rwell ) = ( 1.39e-15 ) ; ( R ) = ( 7.12e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.80e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42407660.45077138 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00655063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119146 +Time: 4.38228e+07s, dt:7446.1s, Cycle: 542 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.20e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.08e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.38e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.45e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 9.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42410041.919952005 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00654653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119101 +Time: 4.38302e+07s, dt:7446.1s, Cycle: 543 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.53e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.30e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.87e-05 ) ; ( Rwell ) = ( 2.99e-15 ) ; ( R ) = ( 1.87e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654891 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119001 +Time: 4.38377e+07s, dt:7446.1s, Cycle: 544 +well_1Control: BHP (at the specified reference elevation): 42412422.66033797 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.54e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 9.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654548 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118931 +Time: 4.38451e+07s, dt:7446.1s, Cycle: 545 +well_1Control: BHP (at the specified reference elevation): 42414801.360029474 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 9.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.94e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.63e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 4.14e-15 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.37e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42417180.66220239 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00654709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118858 +Time: 4.38526e+07s, dt:7446.1s, Cycle: 546 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.64e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 9.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654385 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00118951 +Time: 4.386e+07s, dt:7446.1s, Cycle: 547 +well_1Control: BHP (at the specified reference elevation): 42419558.48038355 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 9.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 9.17e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.12e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.58e-05 ) ; ( Rwell ) = ( 4.30e-15 ) ; ( R ) = ( 1.58e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.12e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42421937.92124064 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00654661 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119193 +Time: 4.38675e+07s, dt:7446.1s, Cycle: 548 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.56e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 9.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119434 +Time: 4.38749e+07s, dt:7446.1s, Cycle: 549 +well_1Control: BHP (at the specified reference elevation): 42424315.5779185 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 9.86e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 9.16e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 1.43e-15 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119632 +Time: 4.38824e+07s, dt:7446.1s, Cycle: 550 +well_1Control: BHP (at the specified reference elevation): 42426694.95607842 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.62e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.90e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 9.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00119842 +Time: 4.38898e+07s, dt:7446.1s, Cycle: 551 +well_1Control: BHP (at the specified reference elevation): 42429072.39019124 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 9.43e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 9.62e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.43e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.99e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 2.29e-15 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654422 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120001 +Time: 4.38973e+07s, dt:7446.1s, Cycle: 552 +well_1Control: BHP (at the specified reference elevation): 42431451.967581645 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.95e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.34e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.62e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.35e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 9.67e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653964 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120165 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.39047e+07s, dt:14892.2s, Cycle: 553 +well_1Control: BHP (at the specified reference elevation): 42433830.44859736 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 5.40e-11 ) ; ( R ) = ( 8.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 4.75e-11 ) ; ( R ) = ( 7.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.47e-03 ) ; ( Rwell ) = ( 4.18e-11 ) ; ( R ) = ( 7.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 6.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.59e-03 ) ; ( Rwell ) = ( 3.22e-11 ) ; ( R ) = ( 6.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.13e-05 ) ; ( Rwell ) = ( 2.17e-15 ) ; ( R ) = ( 3.13e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0130831 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240782 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.39196e+07s, dt:7446.1s, Cycle: 554 +well_1Control: BHP (at the specified reference elevation): 42438588.65039941 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 6.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.37e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.49e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 9.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653738 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120491 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.3927e+07s, dt:14892.2s, Cycle: 555 +well_1Control: BHP (at the specified reference elevation): 42440966.112941094 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 5.43e-11 ) ; ( R ) = ( 8.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 4.78e-11 ) ; ( R ) = ( 8.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 9.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.93e-03 ) ; ( Rwell ) = ( 4.20e-11 ) ; ( R ) = ( 7.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.55e-03 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 7.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 3.25e-11 ) ; ( R ) = ( 7.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 5.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 7.66e-16 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.01308 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00241175 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.39419e+07s, dt:7446.1s, Cycle: 556 +well_1Control: BHP (at the specified reference elevation): 42445722.35022757 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 7.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.15e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120628 +Time: 4.39494e+07s, dt:7446.1s, Cycle: 557 +well_1Control: BHP (at the specified reference elevation): 42448098.40620281 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 9.48e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 9.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 9.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 9.86e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.73e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.83e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.54e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 6.14e-16 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653739 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120614 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.39568e+07s, dt:3723.05s, Cycle: 558 +well_1Control: BHP (at the specified reference elevation): 42450479.92435387 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-04 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 6.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00326848 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00060302 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.39605e+07s, dt:7446.1s, Cycle: 559 +well_1Control: BHP (at the specified reference elevation): 42451668.674989484 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.67e-05 ) ; ( Rwell ) = ( 1.09e-15 ) ; ( R ) = ( 1.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120581 +Time: 4.3968e+07s, dt:7446.1s, Cycle: 560 +well_1Control: BHP (at the specified reference elevation): 42454046.947613634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 7.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.15e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 9.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012056 +Time: 4.39754e+07s, dt:7446.1s, Cycle: 561 +well_1Control: BHP (at the specified reference elevation): 42456424.54576336 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 9.61e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 9.76e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.65e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.22e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 2.43e-15 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.39e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42458802.869591475 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00653561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120481 +Time: 4.39829e+07s, dt:7446.1s, Cycle: 562 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 7.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.18e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.37e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653268 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120413 +Time: 4.39903e+07s, dt:7446.1s, Cycle: 563 +well_1Control: BHP (at the specified reference elevation): 42461179.87833592 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 9.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 9.76e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 8.64e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 2.74e-15 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00653429 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120313 +Time: 4.39978e+07s, dt:2222.17s, Cycle: 564 +well_1Control: BHP (at the specified reference elevation): 42463557.85174 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 2.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 6.26e-13 ) ; ( R ) = ( 7.49e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00195092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000358849 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.4e+07s, dt:4444.34s, Cycle: 565 +well_1Control: BHP (at the specified reference elevation): 42464264.84173243 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.82e-04 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 5.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00390435 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000717404 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.44972e+07, 2.45376e+07, 2.46461e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.19963e+07, 1.21452e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.485 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 18.3756, 719.109 } rm^3 +compflowStatistics, reservoir: Phase mass: { 11100.7, 700721 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1618.9, 215643 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 9481.8, 485077 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 17.1057, 4.76653 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 11083.6, 700716 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 11100.7, 0 }, { 1910.1, 698764 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.42745e+07, 2.44325e+07, 2.45158e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.17736e+07, 1.20149e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.303 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.303 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219396 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65818.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153578 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219396 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27338e-08, 219396 } } kg +well_1Control: BHP (at the specified reference elevation): 42465682.52669095 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 9.30676 +compflowStatistics: Max component CFL number: 12.7892 +Time: 4.40044e+07s, dt:8888.67s, Cycle: 566 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 9.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 9.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 9.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.52e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.33e-05 ) ; ( Rwell ) = ( 5.52e-15 ) ; ( R ) = ( 1.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00780148 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.001433 +Time: 4.40133e+07s, dt:8888.67s, Cycle: 567 +well_1Control: BHP (at the specified reference elevation): 42468518.606610976 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.37e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 9.49e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.37e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.49e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.17e-06 ) ; ( Rwell ) = ( 2.17e-15 ) ; ( R ) = ( 4.17e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00779634 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014307 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.40222e+07s, dt:4444.34s, Cycle: 568 +well_1Control: BHP (at the specified reference elevation): 42471356.89414425 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 6.69e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389829 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00071489 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.40267e+07s, dt:8888.67s, Cycle: 569 +well_1Control: BHP (at the specified reference elevation): 42472773.66633664 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 1.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 8.98e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.92e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.36e-05 ) ; ( Rwell ) = ( 2.96e-16 ) ; ( R ) = ( 2.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00779647 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142682 +Time: 4.40356e+07s, dt:8888.67s, Cycle: 570 +well_1Control: BHP (at the specified reference elevation): 42475611.80664225 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.37e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 7.26e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.01e-06 ) ; ( Rwell ) = ( 1.62e-15 ) ; ( R ) = ( 7.01e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42478449.84501058 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00779347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142388 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.40444e+07s, dt:4444.34s, Cycle: 571 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 6.28e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0038972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000711169 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.40489e+07s, dt:8888.67s, Cycle: 572 +well_1Control: BHP (at the specified reference elevation): 42479866.45329582 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 9.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 9.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 9.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 9.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.35e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.68e-05 ) ; ( Rwell ) = ( 2.16e-15 ) ; ( R ) = ( 1.68e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42482702.27070454 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00779534 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141909 +Time: 4.40578e+07s, dt:8888.67s, Cycle: 573 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.32e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.70e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 6.28e-06 ) ; ( Rwell ) = ( 1.72e-15 ) ; ( R ) = ( 6.28e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00779135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141542 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.40667e+07s, dt:4444.34s, Cycle: 574 +well_1Control: BHP (at the specified reference elevation): 42485539.338436544 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 6.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389602 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000706842 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.40711e+07s, dt:8888.67s, Cycle: 575 +well_1Control: BHP (at the specified reference elevation): 42486955.28368463 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.54e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.84e-05 ) ; ( Rwell ) = ( 2.34e-15 ) ; ( R ) = ( 1.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.31e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42489782.83337067 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00779667 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140947 +Time: 4.408e+07s, dt:8888.67s, Cycle: 576 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 9.84e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 8.67e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.63e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.72e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.93e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.97e-06 ) ; ( Rwell ) = ( 6.25e-16 ) ; ( R ) = ( 4.97e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778977 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140827 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.40889e+07s, dt:4444.34s, Cycle: 577 +well_1Control: BHP (at the specified reference elevation): 42492614.173903376 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 5.09e-12 ) ; ( R ) = ( 6.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389503 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000703701 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.40933e+07s, dt:8888.67s, Cycle: 578 +well_1Control: BHP (at the specified reference elevation): 42494027.60254568 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 8.23e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.29e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.31e-06 ) ; ( Rwell ) = ( 7.77e-16 ) ; ( R ) = ( 4.31e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00779191 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140644 +Time: 4.41022e+07s, dt:8888.67s, Cycle: 579 +well_1Control: BHP (at the specified reference elevation): 42496857.86164835 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 9.51e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 8.46e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 8.85e-06 ) ; ( Rwell ) = ( 2.88e-16 ) ; ( R ) = ( 8.85e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778712 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140554 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.41111e+07s, dt:4444.34s, Cycle: 580 +well_1Control: BHP (at the specified reference elevation): 42499689.83568421 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 6.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000702712 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.41156e+07s, dt:8888.67s, Cycle: 581 +well_1Control: BHP (at the specified reference elevation): 42501103.6747867 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 9.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 9.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 9.97e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 8.86e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.00e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.81e-05 ) ; ( Rwell ) = ( 1.34e-15 ) ; ( R ) = ( 1.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778995 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140419 +Time: 4.41244e+07s, dt:8888.67s, Cycle: 582 +well_1Control: BHP (at the specified reference elevation): 42503933.30156745 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 1.02e-12 ) ; ( R ) = ( 7.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778404 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140598 +Time: 4.41333e+07s, dt:8888.67s, Cycle: 583 +well_1Control: BHP (at the specified reference elevation): 42506763.61274745 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 9.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 8.06e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 3.74e-16 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778413 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140721 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.41422e+07s, dt:4444.34s, Cycle: 584 +well_1Control: BHP (at the specified reference elevation): 42509594.551801294 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 6.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000703817 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.41467e+07s, dt:8888.67s, Cycle: 585 +well_1Control: BHP (at the specified reference elevation): 42511008.4413677 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 9.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.08e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.52e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.32e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.74e-05 ) ; ( Rwell ) = ( 6.49e-16 ) ; ( R ) = ( 1.74e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.007786 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140859 +Time: 4.41556e+07s, dt:8888.67s, Cycle: 586 +well_1Control: BHP (at the specified reference elevation): 42513837.95544739 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 7.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 8.53e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.52e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.16e-05 ) ; ( Rwell ) = ( 8.10e-16 ) ; ( R ) = ( 1.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778131 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140914 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.41644e+07s, dt:4444.34s, Cycle: 587 +well_1Control: BHP (at the specified reference elevation): 42516669.65739466 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 5.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42518083.49116027 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00389094 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000704853 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.41689e+07s, dt:8888.67s, Cycle: 588 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 9.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 9.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 8.92e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.52e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.93e-05 ) ; ( Rwell ) = ( 1.09e-15 ) ; ( R ) = ( 1.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00778388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140951 +Time: 4.41778e+07s, dt:8888.67s, Cycle: 589 +well_1Control: BHP (at the specified reference elevation): 42520913.22189076 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.22e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 9.93e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 8.73e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.07e-05 ) ; ( Rwell ) = ( 2.05e-16 ) ; ( R ) = ( 2.07e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777892 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140926 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.41867e+07s, dt:4444.34s, Cycle: 590 +well_1Control: BHP (at the specified reference elevation): 42523744.767892234 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-04 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-04 ) ; ( Rwell ) = ( 9.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-04 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.93e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-04 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.66e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-04 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.43e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.23e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.04e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.99e-13 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 7.76e-13 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 6.73e-13 ) ; ( R ) = ( 9.41e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00070478 +Time: 4.41911e+07s, dt:4444.34s, Cycle: 591 +well_1Control: BHP (at the specified reference elevation): 42525157.53877133 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 9.43e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 9.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 8.10e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00390074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000704529 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.41956e+07s, dt:8888.67s, Cycle: 592 +well_1Control: BHP (at the specified reference elevation): 42526570.499270655 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 9.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 9.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.82e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 7.77e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.15e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.03e-05 ) ; ( Rwell ) = ( 1.42e-15 ) ; ( R ) = ( 2.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777936 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140787 +Time: 4.42044e+07s, dt:8888.67s, Cycle: 593 +well_1Control: BHP (at the specified reference elevation): 42529401.42956634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 8.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 8.75e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.73e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.83e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.74e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.64e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.32e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 5.87e-16 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140661 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.42133e+07s, dt:4444.34s, Cycle: 594 +well_1Control: BHP (at the specified reference elevation): 42532232.90946379 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 5.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388847 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000703126 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42178e+07s, dt:8888.67s, Cycle: 595 +well_1Control: BHP (at the specified reference elevation): 42533644.99600959 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.14e-05 ) ; ( Rwell ) = ( 1.94e-15 ) ; ( R ) = ( 2.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140476 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.42267e+07s, dt:4444.34s, Cycle: 596 +well_1Control: BHP (at the specified reference elevation): 42536474.560220525 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 6.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0038872 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000703098 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42311e+07s, dt:8888.67s, Cycle: 597 +well_1Control: BHP (at the specified reference elevation): 42537887.43814184 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 9.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 8.96e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.73e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.68e-05 ) ; ( Rwell ) = ( 4.12e-15 ) ; ( R ) = ( 2.68e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140962 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.424e+07s, dt:4444.34s, Cycle: 598 +well_1Control: BHP (at the specified reference elevation): 42540714.92858555 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-04 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 4.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 6.48e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000706285 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42444e+07s, dt:8888.67s, Cycle: 599 +well_1Control: BHP (at the specified reference elevation): 42542126.57260031 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 9.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 6.22e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.34e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 7.72e-16 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777648 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014159 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.42533e+07s, dt:4444.34s, Cycle: 600 +well_1Control: BHP (at the specified reference elevation): 42544953.595563605 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 5.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388596 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000709549 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42578e+07s, dt:8888.67s, Cycle: 601 +well_1Control: BHP (at the specified reference elevation): 42546365.39374058 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 9.61e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.98e-05 ) ; ( Rwell ) = ( 3.69e-15 ) ; ( R ) = ( 1.98e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777605 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142064 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.42667e+07s, dt:4444.34s, Cycle: 602 +well_1Control: BHP (at the specified reference elevation): 42549191.134536885 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 5.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42550603.58284882 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00388485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000711462 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42711e+07s, dt:8888.67s, Cycle: 603 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 9.02e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.51e-05 ) ; ( Rwell ) = ( 2.46e-17 ) ; ( R ) = ( 1.51e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00777413 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142552 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.428e+07s, dt:4444.34s, Cycle: 604 +well_1Control: BHP (at the specified reference elevation): 42553428.80991411 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 5.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42554840.72031279 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00388423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000713946 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42844e+07s, dt:8888.67s, Cycle: 605 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 9.23e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 6.39e-06 ) ; ( Rwell ) = ( 7.76e-16 ) ; ( R ) = ( 6.39e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0077724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142942 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.42933e+07s, dt:4444.34s, Cycle: 606 +well_1Control: BHP (at the specified reference elevation): 42557665.97128655 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 5.53e-12 ) ; ( R ) = ( 6.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388364 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000714941 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.42978e+07s, dt:8888.67s, Cycle: 607 +well_1Control: BHP (at the specified reference elevation): 42559076.22072882 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 9.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 9.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 9.55e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.57e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 9.59e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 9.59e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 1.70e-15 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00776881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143154 +Time: 4.43067e+07s, dt:8888.67s, Cycle: 608 +well_1Control: BHP (at the specified reference elevation): 42561903.23800291 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 9.89e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 1.18e-15 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00776476 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014333 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.43155e+07s, dt:4444.34s, Cycle: 609 +well_1Control: BHP (at the specified reference elevation): 42564728.23074327 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-04 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 7.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42566139.44518399 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00388241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000717104 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.432e+07s, dt:8888.67s, Cycle: 610 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 9.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 7.85e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.22e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 1.74e-15 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00776435 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143532 +Time: 4.43289e+07s, dt:8888.67s, Cycle: 611 +well_1Control: BHP (at the specified reference elevation): 42568963.578642204 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.42e-05 ) ; ( Rwell ) = ( 6.49e-16 ) ; ( R ) = ( 1.42e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00776196 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143615 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.43378e+07s, dt:4444.34s, Cycle: 612 +well_1Control: BHP (at the specified reference elevation): 42571788.18652977 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 5.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388182 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000718524 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.43422e+07s, dt:8888.67s, Cycle: 613 +well_1Control: BHP (at the specified reference elevation): 42573195.785091475 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 8.79e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 7.74e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.82e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.66e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.83e-05 ) ; ( Rwell ) = ( 3.69e-17 ) ; ( R ) = ( 1.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00776532 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143672 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.43511e+07s, dt:4444.34s, Cycle: 614 +well_1Control: BHP (at the specified reference elevation): 42576019.426801406 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.66e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-04 ) ; ( Rwell ) = ( 9.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-04 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.28e-04 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 4.28e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000718413 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.43555e+07s, dt:8888.67s, Cycle: 615 +well_1Control: BHP (at the specified reference elevation): 42577429.21430076 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 9.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 8.82e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.77e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.84e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.14e-05 ) ; ( Rwell ) = ( 1.81e-16 ) ; ( R ) = ( 1.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00776203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143654 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.43644e+07s, dt:4444.34s, Cycle: 616 +well_1Control: BHP (at the specified reference elevation): 42580252.041064665 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.61e-04 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 5.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42581660.45914065 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00387975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000718573 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.43689e+07s, dt:8888.67s, Cycle: 617 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 9.26e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.63e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 1.94e-15 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42584482.44281278 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00776188 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143588 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.43778e+07s, dt:4444.34s, Cycle: 618 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 5.63e-12 ) ; ( R ) = ( 6.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0038792 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000717835 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.43822e+07s, dt:8888.67s, Cycle: 619 +well_1Control: BHP (at the specified reference elevation): 42585889.167735204 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 9.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 9.83e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 8.71e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.30e-06 ) ; ( Rwell ) = ( 4.81e-15 ) ; ( R ) = ( 3.30e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.69e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42588712.03513312 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00775996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143442 +Time: 4.43911e+07s, dt:8888.67s, Cycle: 620 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.38e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 9.98e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 8.82e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.94e-05 ) ; ( Rwell ) = ( 1.76e-15 ) ; ( R ) = ( 1.94e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775542 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143311 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.44e+07s, dt:4444.34s, Cycle: 621 +well_1Control: BHP (at the specified reference elevation): 42591535.11091009 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 7.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000716418 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.44044e+07s, dt:8888.67s, Cycle: 622 +well_1Control: BHP (at the specified reference elevation): 42592943.00767243 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.56e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.10e-06 ) ; ( Rwell ) = ( 5.90e-15 ) ; ( R ) = ( 6.10e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143064 +Time: 4.44133e+07s, dt:8888.67s, Cycle: 623 +well_1Control: BHP (at the specified reference elevation): 42595766.4158594 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.37e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 8.14e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.93e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.52e-06 ) ; ( Rwell ) = ( 2.64e-15 ) ; ( R ) = ( 1.52e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775272 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142855 +Time: 4.44222e+07s, dt:8888.67s, Cycle: 624 +well_1Control: BHP (at the specified reference elevation): 42598590.49436508 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.37e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 8.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.04e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.64e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.50e-06 ) ; ( Rwell ) = ( 2.09e-15 ) ; ( R ) = ( 3.50e-06 ) ; + Last LinSolve(iter,res) = ( 6, 6.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142621 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.44311e+07s, dt:4444.34s, Cycle: 625 +well_1Control: BHP (at the specified reference elevation): 42601414.597968884 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 5.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387623 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00071274 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.44355e+07s, dt:8888.67s, Cycle: 626 +well_1Control: BHP (at the specified reference elevation): 42602823.07688022 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 9.57e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 7.54e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.86e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.19e-05 ) ; ( Rwell ) = ( 1.39e-16 ) ; ( R ) = ( 1.19e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775603 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142244 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.44444e+07s, dt:4444.34s, Cycle: 627 +well_1Control: BHP (at the specified reference elevation): 42605644.65796511 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 6.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387501 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000710682 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.44489e+07s, dt:8888.67s, Cycle: 628 +well_1Control: BHP (at the specified reference elevation): 42607052.66519145 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 9.79e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.69e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.85e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.78e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.98e-06 ) ; ( Rwell ) = ( 2.77e-15 ) ; ( R ) = ( 9.98e-06 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141784 +Time: 4.44578e+07s, dt:8888.67s, Cycle: 629 +well_1Control: BHP (at the specified reference elevation): 42609875.348722994 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.33e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.51e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.14e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.57e-06 ) ; ( Rwell ) = ( 1.30e-15 ) ; ( R ) = ( 8.57e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0077479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141428 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.44667e+07s, dt:4444.34s, Cycle: 630 +well_1Control: BHP (at the specified reference elevation): 42612698.260524124 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 6.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387399 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000706406 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.44711e+07s, dt:8888.67s, Cycle: 631 +well_1Control: BHP (at the specified reference elevation): 42614105.49037622 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 9.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 9.26e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.54e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.35e-06 ) ; ( Rwell ) = ( 2.79e-15 ) ; ( R ) = ( 8.35e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00774816 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140875 +Time: 4.448e+07s, dt:8888.67s, Cycle: 632 +well_1Control: BHP (at the specified reference elevation): 42616928.825371414 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 8.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 7.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 8.90e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.18e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.31e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.20e-05 ) ; ( Rwell ) = ( 3.20e-15 ) ; ( R ) = ( 1.20e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.12e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42619751.29005104 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0077449 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140495 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.44889e+07s, dt:4444.34s, Cycle: 633 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 6.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387286 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00070173 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.44933e+07s, dt:8888.67s, Cycle: 634 +well_1Control: BHP (at the specified reference elevation): 42621159.00737992 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.35e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 7.40e-12 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.17e-05 ) ; ( Rwell ) = ( 4.14e-15 ) ; ( R ) = ( 2.17e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00774747 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00139854 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.45022e+07s, dt:4444.34s, Cycle: 635 +well_1Control: BHP (at the specified reference elevation): 42623980.01606423 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 6.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387187 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000698385 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.45067e+07s, dt:8888.67s, Cycle: 636 +well_1Control: BHP (at the specified reference elevation): 42625389.05539431 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.75e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 8.02e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.26e-05 ) ; ( Rwell ) = ( 1.85e-15 ) ; ( R ) = ( 1.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00774682 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00139978 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.45155e+07s, dt:4444.34s, Cycle: 637 +well_1Control: BHP (at the specified reference elevation): 42628208.914341524 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 5.35e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000700848 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.452e+07s, dt:8888.67s, Cycle: 638 +well_1Control: BHP (at the specified reference elevation): 42629617.948314816 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 6.98e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.42e-06 ) ; ( Rwell ) = ( 8.36e-16 ) ; ( R ) = ( 4.42e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00774519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140463 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.45289e+07s, dt:4444.34s, Cycle: 639 +well_1Control: BHP (at the specified reference elevation): 42632438.268672556 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 7.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000703083 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.45333e+07s, dt:8888.67s, Cycle: 640 +well_1Control: BHP (at the specified reference elevation): 42633844.71131848 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 9.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 8.92e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.18e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.13e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 5.97e-15 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42636667.820847 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00774207 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140803 +Time: 4.45422e+07s, dt:8888.67s, Cycle: 641 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 8.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 8.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 9.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 8.14e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.31e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.59e-06 ) ; ( Rwell ) = ( 3.80e-15 ) ; ( R ) = ( 3.59e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42639487.381853744 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00773821 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00140979 +Time: 4.45511e+07s, dt:8888.67s, Cycle: 642 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.02e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.57e-05 ) ; ( Rwell ) = ( 9.35e-16 ) ; ( R ) = ( 1.57e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42642306.79533917 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00773693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141103 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.456e+07s, dt:4444.34s, Cycle: 643 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 6.98e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00386898 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000705807 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.45644e+07s, dt:8888.67s, Cycle: 644 +well_1Control: BHP (at the specified reference elevation): 42643712.47624549 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.49e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 8.40e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.84e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 1.31e-15 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00773785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141372 +Time: 4.45733e+07s, dt:8888.67s, Cycle: 645 +well_1Control: BHP (at the specified reference elevation): 42646531.750100404 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 9.73e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.59e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.58e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.00e-06 ) ; ( Rwell ) = ( 2.84e-15 ) ; ( R ) = ( 5.00e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00773462 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141732 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.45822e+07s, dt:4444.34s, Cycle: 646 +well_1Control: BHP (at the specified reference elevation): 42649350.35441579 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 6.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00386779 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000709499 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.45867e+07s, dt:8888.67s, Cycle: 647 +well_1Control: BHP (at the specified reference elevation): 42650754.099777 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 9.07e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.26e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 4.10e-16 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00773585 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142205 +Time: 4.45955e+07s, dt:8888.67s, Cycle: 648 +well_1Control: BHP (at the specified reference elevation): 42653573.14113447 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 7.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 8.78e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.76e-06 ) ; ( Rwell ) = ( 3.93e-16 ) ; ( R ) = ( 8.76e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00773245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142489 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.46044e+07s, dt:4444.34s, Cycle: 649 +well_1Control: BHP (at the specified reference elevation): 42656391.171643905 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 6.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42657797.40336239 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00386653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000713129 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.46089e+07s, dt:8888.67s, Cycle: 650 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.48e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.54e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 2.96e-15 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0077342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142851 +Time: 4.46178e+07s, dt:8888.67s, Cycle: 651 +well_1Control: BHP (at the specified reference elevation): 42660614.35051453 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.30e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 9.53e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 7.46e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.19e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.00e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.15e-05 ) ; ( Rwell ) = ( 1.73e-15 ) ; ( R ) = ( 1.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00772989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143043 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.46267e+07s, dt:4444.34s, Cycle: 652 +well_1Control: BHP (at the specified reference elevation): 42663431.8441443 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 7.00e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00386527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000715699 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.46311e+07s, dt:8888.67s, Cycle: 653 +well_1Control: BHP (at the specified reference elevation): 42664837.69167718 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.53e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 8.41e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 2.42e-16 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.26e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42667653.589453846 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00773225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143291 +Time: 4.464e+07s, dt:8888.67s, Cycle: 654 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.34e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 9.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 8.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 1.63e-15 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42670470.24403046 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00772747 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143514 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.46489e+07s, dt:4444.34s, Cycle: 655 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 5.97e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00386381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000718618 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.46533e+07s, dt:8888.67s, Cycle: 656 +well_1Control: BHP (at the specified reference elevation): 42671875.555665955 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 9.12e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 7.13e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.47e-05 ) ; ( Rwell ) = ( 6.38e-15 ) ; ( R ) = ( 2.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42674692.99758478 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00772761 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144034 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.46622e+07s, dt:4444.34s, Cycle: 657 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 6.42e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00386296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000720963 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.46667e+07s, dt:8888.67s, Cycle: 658 +well_1Control: BHP (at the specified reference elevation): 42676099.06565818 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 7.94e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.53e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.46e-05 ) ; ( Rwell ) = ( 4.72e-15 ) ; ( R ) = ( 2.46e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00772696 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144536 +Time: 4.46755e+07s, dt:8888.67s, Cycle: 659 +well_1Control: BHP (at the specified reference elevation): 42678915.771636456 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.39e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 8.33e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.35e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.48e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.67e-05 ) ; ( Rwell ) = ( 3.32e-15 ) ; ( R ) = ( 1.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42681732.55115154 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00772334 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144861 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.46844e+07s, dt:4444.34s, Cycle: 660 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 6.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42683136.16058112 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0038619 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000725195 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.46889e+07s, dt:8888.67s, Cycle: 661 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 9.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 9.55e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 8.39e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 5.56e-15 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00772488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145285 +Time: 4.46978e+07s, dt:8888.67s, Cycle: 662 +well_1Control: BHP (at the specified reference elevation): 42685952.71797237 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.45e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 8.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.82e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.98e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.36e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.25e-05 ) ; ( Rwell ) = ( 7.17e-16 ) ; ( R ) = ( 1.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.38e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42688768.470152445 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00772093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145526 +Time: 4.47066e+07s, dt:8888.67s, Cycle: 663 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.47e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 9.02e-12 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.51e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.34e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.19e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00771932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145737 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.47155e+07s, dt:4444.34s, Cycle: 664 +well_1Control: BHP (at the specified reference elevation): 42691582.53419037 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 7.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385862 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000729212 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.472e+07s, dt:8888.67s, Cycle: 665 +well_1Control: BHP (at the specified reference elevation): 42692986.954392105 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 9.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 8.75e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.74e-05 ) ; ( Rwell ) = ( 1.60e-15 ) ; ( R ) = ( 2.74e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00772146 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146016 +Time: 4.47289e+07s, dt:8888.67s, Cycle: 666 +well_1Control: BHP (at the specified reference elevation): 42695800.154428676 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 8.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 7.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 1.83e-15 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00771751 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146146 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.47378e+07s, dt:4444.34s, Cycle: 667 +well_1Control: BHP (at the specified reference elevation): 42698614.81837267 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 5.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385902 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000731082 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.47422e+07s, dt:8888.67s, Cycle: 668 +well_1Control: BHP (at the specified reference elevation): 42700020.4147295 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.39e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.76e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.76e-05 ) ; ( Rwell ) = ( 5.02e-15 ) ; ( R ) = ( 2.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00772028 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146291 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.47511e+07s, dt:4444.34s, Cycle: 669 +well_1Control: BHP (at the specified reference elevation): 42702833.02132798 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 6.13e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385792 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000731641 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.47555e+07s, dt:8888.67s, Cycle: 670 +well_1Control: BHP (at the specified reference elevation): 42704238.585050225 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.86e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.65e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.93e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.97e-06 ) ; ( Rwell ) = ( 4.95e-16 ) ; ( R ) = ( 3.97e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00771901 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146279 +Time: 4.47644e+07s, dt:8888.67s, Cycle: 671 +well_1Control: BHP (at the specified reference elevation): 42707051.61949693 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 9.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 7.66e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.75e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 1.75e-15 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42709867.00995238 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00771406 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146145 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.47733e+07s, dt:4444.34s, Cycle: 672 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 6.00e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385701 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000730577 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.47778e+07s, dt:8888.67s, Cycle: 673 +well_1Control: BHP (at the specified reference elevation): 42711273.54950992 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.28e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 9.64e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 8.47e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 8.27e-16 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00771596 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146042 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.47866e+07s, dt:4444.34s, Cycle: 674 +well_1Control: BHP (at the specified reference elevation): 42714084.182840005 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 5.00e-12 ) ; ( R ) = ( 6.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000730061 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.47911e+07s, dt:8888.67s, Cycle: 675 +well_1Control: BHP (at the specified reference elevation): 42715488.446859986 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.37e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.43e-06 ) ; ( Rwell ) = ( 1.96e-16 ) ; ( R ) = ( 5.43e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00771609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014591 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48e+07s, dt:4444.34s, Cycle: 676 +well_1Control: BHP (at the specified reference elevation): 42718298.16455035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 5.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385531 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000729403 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.48044e+07s, dt:8888.67s, Cycle: 677 +well_1Control: BHP (at the specified reference elevation): 42719701.415208526 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 9.44e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 8.37e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.85e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.88e-05 ) ; ( Rwell ) = ( 5.85e-15 ) ; ( R ) = ( 1.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00771563 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145716 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48133e+07s, dt:4444.34s, Cycle: 678 +well_1Control: BHP (at the specified reference elevation): 42722512.25416738 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 6.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000728148 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.48178e+07s, dt:8888.67s, Cycle: 679 +well_1Control: BHP (at the specified reference elevation): 42723914.94443168 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 8.52e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 7.50e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.13e-05 ) ; ( Rwell ) = ( 9.29e-16 ) ; ( R ) = ( 2.13e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0077121 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145457 +Time: 4.48266e+07s, dt:8888.67s, Cycle: 680 +well_1Control: BHP (at the specified reference elevation): 42726727.35474281 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 8.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 9.63e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.63e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.86e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.47e-05 ) ; ( Rwell ) = ( 6.79e-16 ) ; ( R ) = ( 1.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42729540.302908875 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00770769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145399 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48355e+07s, dt:4444.34s, Cycle: 681 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 4.89e-12 ) ; ( R ) = ( 5.05e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000726819 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.484e+07s, dt:8888.67s, Cycle: 682 +well_1Control: BHP (at the specified reference elevation): 42730944.96057919 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.04e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 7.99e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.52e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.04e-05 ) ; ( Rwell ) = ( 1.39e-16 ) ; ( R ) = ( 2.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00770988 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145264 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48489e+07s, dt:4444.34s, Cycle: 683 +well_1Control: BHP (at the specified reference elevation): 42733756.14966987 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-04 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 5.47e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42735160.355558895 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00385281 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000726126 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.48533e+07s, dt:8888.67s, Cycle: 684 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 7.10e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.93e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 1.98e-15 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00770882 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145084 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48622e+07s, dt:4444.34s, Cycle: 685 +well_1Control: BHP (at the specified reference elevation): 42737971.051588856 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 5.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385196 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000725139 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.48666e+07s, dt:8888.67s, Cycle: 686 +well_1Control: BHP (at the specified reference elevation): 42739375.2158155 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 8.22e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 7.28e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 6.87e-15 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.57e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42742185.463306814 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00770769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144826 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48755e+07s, dt:4444.34s, Cycle: 687 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 6.32e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000723736 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.488e+07s, dt:8888.67s, Cycle: 688 +well_1Control: BHP (at the specified reference elevation): 42743589.47534403 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.98e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.33e-05 ) ; ( Rwell ) = ( 6.15e-15 ) ; ( R ) = ( 1.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00770588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144495 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.48889e+07s, dt:4444.34s, Cycle: 689 +well_1Control: BHP (at the specified reference elevation): 42746399.17192552 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.24e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 5.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.92e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42747800.959153466 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00385039 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000721965 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.48933e+07s, dt:8888.67s, Cycle: 690 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 9.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 8.98e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.15e-06 ) ; ( Rwell ) = ( 8.88e-16 ) ; ( R ) = ( 8.15e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00770231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144676 +Time: 4.49022e+07s, dt:8888.67s, Cycle: 691 +well_1Control: BHP (at the specified reference elevation): 42750613.69944386 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 8.47e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 8.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 9.62e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.51e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.52e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.90e-06 ) ; ( Rwell ) = ( 4.91e-17 ) ; ( R ) = ( 7.90e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00769893 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144976 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.49111e+07s, dt:4444.34s, Cycle: 692 +well_1Control: BHP (at the specified reference elevation): 42753425.67255591 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 6.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42754830.72979912 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00384981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000725715 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.49155e+07s, dt:8888.67s, Cycle: 693 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.30e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.26e-05 ) ; ( Rwell ) = ( 1.91e-15 ) ; ( R ) = ( 2.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00770063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145354 +Time: 4.49244e+07s, dt:8888.67s, Cycle: 694 +well_1Control: BHP (at the specified reference elevation): 42757640.03402911 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 8.46e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 9.55e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.54e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.67e-05 ) ; ( Rwell ) = ( 2.29e-15 ) ; ( R ) = ( 1.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00769656 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145564 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.49333e+07s, dt:4444.34s, Cycle: 695 +well_1Control: BHP (at the specified reference elevation): 42760451.48218116 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-04 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.24e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00384842 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000728388 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.49378e+07s, dt:8888.67s, Cycle: 696 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 42761856.70262762 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 7.98e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 7.03e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 6.54e-15 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00769909 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145809 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.49466e+07s, dt:4444.34s, Cycle: 697 +well_1Control: BHP (at the specified reference elevation): 42764666.8413077 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 5.72e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00384735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000729453 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.49511e+07s, dt:8888.67s, Cycle: 698 +well_1Control: BHP (at the specified reference elevation): 42766072.11599907 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 9.01e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.92e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.78e-05 ) ; ( Rwell ) = ( 5.82e-15 ) ; ( R ) = ( 2.78e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00769786 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145992 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.496e+07s, dt:4444.34s, Cycle: 699 +well_1Control: BHP (at the specified reference elevation): 42768881.86284719 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 5.41e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00384666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000730238 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.49644e+07s, dt:8888.67s, Cycle: 700 +well_1Control: BHP (at the specified reference elevation): 42770286.517864734 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.36e-05 ) ; ( Rwell ) = ( 1.30e-15 ) ; ( R ) = ( 2.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00769706 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146075 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.49733e+07s, dt:4444.34s, Cycle: 701 +well_1Control: BHP (at the specified reference elevation): 42773095.665024 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 6.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42774499.630473584 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00384612 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000730577 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.49778e+07s, dt:8888.67s, Cycle: 702 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.69e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 7.66e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.76e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.40e-05 ) ; ( Rwell ) = ( 1.22e-15 ) ; ( R ) = ( 1.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00769458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146088 +Time: 4.49866e+07s, dt:8888.67s, Cycle: 703 +well_1Control: BHP (at the specified reference elevation): 42777308.70486292 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 8.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.61e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 1.80e-15 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42780119.6802268 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00769026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146058 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.49955e+07s, dt:4444.34s, Cycle: 704 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 6.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00384516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000730128 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.5e+07s, dt:24.4958s, Cycle: 705 +well_1Control: BHP (at the specified reference elevation): 42781523.91796437 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 2.56e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-05 ) ; ( Rwell ) = ( 2.41e-13 ) ; ( R ) = ( 2.18e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.73e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42781531.631783925 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00896555 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000233709 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.5e+07s, dt:48.9916s, Cycle: 706 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 5.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-06 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 4.61e-06 ) ; + Last LinSolve(iter,res) = ( 3, 2.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00856721 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 8.04249e-06 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +well_1Control: BHP (at the specified reference elevation): 42781547.06447953 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.47075e+07, 2.47479e+07, 2.48565e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.22075e+07, 1.23565e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.638 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 18.6928, 718.945 } rm^3 +compflowStatistics, reservoir: Phase mass: { 11360.8, 700676 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1654.42, 215725 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 9706.34, 484951 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 17.6473, 5.63027 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 11343.1, 700671 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 11360.8, 0 }, { 1944.42, 698684 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.44859e+07, 2.46431e+07, 2.47261e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.19859e+07, 1.22261e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.35 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.35 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219476 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65842.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153633 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219476 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27421e-08, 219476 } } kg +compflowStatistics: Max phase CFL number: 0.101958 +compflowStatistics: Max component CFL number: 0.140114 +Time: 4.5e+07s, dt:97.9833s, Cycle: 707 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.27e-05 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.27e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.15e-06 ) ; ( Rwell ) = ( 9.64e-13 ) ; ( R ) = ( 9.15e-06 ) ; + Last LinSolve(iter,res) = ( 3, 3.48e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42781577.93922796 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.000196336 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 1.60937e-05 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50001e+07s, dt:195.967s, Cycle: 708 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.89e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-05 ) ; ( Rwell ) = ( 2.71e-13 ) ; ( R ) = ( 2.35e-05 ) ; + Last LinSolve(iter,res) = ( 3, 3.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.000171003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 3.21944e-05 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50003e+07s, dt:391.933s, Cycle: 709 +well_1Control: BHP (at the specified reference elevation): 42781639.71346138 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-05 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.71e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.08e-05 ) ; ( Rwell ) = ( 1.36e-12 ) ; ( R ) = ( 7.08e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.44e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42781763.19064611 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.000379578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 6.44013e-05 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50007e+07s, dt:783.866s, Cycle: 710 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.42e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.42e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-04 ) ; ( Rwell ) = ( 1.78e-12 ) ; ( R ) = ( 2.01e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42782010.8233123 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.000712482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000128815 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50015e+07s, dt:1567.73s, Cycle: 711 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.02e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 8.64e-13 ) ; ( R ) = ( 5.18e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.64e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42782505.34621549 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00140148 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000257731 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50031e+07s, dt:3135.46s, Cycle: 712 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 7.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0027418 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000515009 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50062e+07s, dt:6270.93s, Cycle: 713 +well_1Control: BHP (at the specified reference elevation): 42783494.085048854 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 9.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0054248 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102944 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.50125e+07s, dt:12541.9s, Cycle: 714 +well_1Control: BHP (at the specified reference elevation): 42785473.83061565 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.66e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 8.59e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.59e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.93e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.14e-05 ) ; ( Rwell ) = ( 7.46e-15 ) ; ( R ) = ( 2.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.91e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42789432.95531061 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.010849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205611 +Time: 4.5025e+07s, dt:12541.9s, Cycle: 715 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.76e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 8.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.89e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.95e-05 ) ; ( Rwell ) = ( 2.32e-16 ) ; ( R ) = ( 1.95e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205215 +Time: 4.50376e+07s, dt:12541.9s, Cycle: 716 +well_1Control: BHP (at the specified reference elevation): 42793392.43101865 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.76e-11 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.00e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.26e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.90e-06 ) ; ( Rwell ) = ( 9.62e-16 ) ; ( R ) = ( 8.90e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108429 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204695 +Time: 4.50501e+07s, dt:12541.9s, Cycle: 717 +well_1Control: BHP (at the specified reference elevation): 42797351.39282037 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 3.80e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.84e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.81e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.90e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.26e-06 ) ; ( Rwell ) = ( 7.11e-15 ) ; ( R ) = ( 6.26e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108412 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204183 +Time: 4.50627e+07s, dt:12541.9s, Cycle: 718 +well_1Control: BHP (at the specified reference elevation): 42801310.19745908 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.76e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 8.94e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.99e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.15e-06 ) ; ( Rwell ) = ( 4.33e-15 ) ; ( R ) = ( 4.15e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108397 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00203611 +Time: 4.50752e+07s, dt:12541.9s, Cycle: 719 +well_1Control: BHP (at the specified reference elevation): 42805268.84336513 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.77e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 9.75e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.65e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.62e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.30e-06 ) ; ( Rwell ) = ( 2.46e-16 ) ; ( R ) = ( 3.30e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108379 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202742 +Time: 4.50877e+07s, dt:12541.9s, Cycle: 720 +well_1Control: BHP (at the specified reference elevation): 42809227.75282499 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.88e-06 ) ; ( Rwell ) = ( 9.53e-16 ) ; ( R ) = ( 9.88e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.010836 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00201935 +Time: 4.51003e+07s, dt:12541.9s, Cycle: 721 +well_1Control: BHP (at the specified reference elevation): 42813186.67045636 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.74e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 7.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 8.86e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.75e-06 ) ; ( Rwell ) = ( 1.60e-15 ) ; ( R ) = ( 3.75e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020111 +Time: 4.51128e+07s, dt:12541.9s, Cycle: 722 +well_1Control: BHP (at the specified reference elevation): 42817145.76143849 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.74e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.89e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.39e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 2.79e-15 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00200764 +Time: 4.51254e+07s, dt:12541.9s, Cycle: 723 +well_1Control: BHP (at the specified reference elevation): 42821104.509247445 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.77e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 9.99e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.38e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.33e-05 ) ; ( Rwell ) = ( 1.51e-16 ) ; ( R ) = ( 1.33e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108307 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00200668 +Time: 4.51379e+07s, dt:12541.9s, Cycle: 724 +well_1Control: BHP (at the specified reference elevation): 42825062.36512507 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.68e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.75e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.73e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.97e-06 ) ; ( Rwell ) = ( 4.75e-16 ) ; ( R ) = ( 6.97e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00200513 +Time: 4.51505e+07s, dt:12541.9s, Cycle: 725 +well_1Control: BHP (at the specified reference elevation): 42829020.40808022 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.74e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 9.95e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.73e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 4.74e-15 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108271 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020027 +Time: 4.5163e+07s, dt:12541.9s, Cycle: 726 +well_1Control: BHP (at the specified reference elevation): 42832978.86621104 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.70e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.77e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.61e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 3.99e-15 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199935 +Time: 4.51755e+07s, dt:12541.9s, Cycle: 727 +well_1Control: BHP (at the specified reference elevation): 42836937.4555105 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 9.50e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.48e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.45e-05 ) ; ( Rwell ) = ( 3.10e-16 ) ; ( R ) = ( 1.45e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108236 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199803 +Time: 4.51881e+07s, dt:12541.9s, Cycle: 728 +well_1Control: BHP (at the specified reference elevation): 42840896.117608175 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.66e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.92e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.70e-05 ) ; ( Rwell ) = ( 4.58e-15 ) ; ( R ) = ( 1.70e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108219 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199623 +Time: 4.52006e+07s, dt:12541.9s, Cycle: 729 +well_1Control: BHP (at the specified reference elevation): 42844854.79395534 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 9.72e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 8.58e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.56e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.26e-05 ) ; ( Rwell ) = ( 4.94e-15 ) ; ( R ) = ( 1.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108202 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199639 +Time: 4.52132e+07s, dt:12541.9s, Cycle: 730 +well_1Control: BHP (at the specified reference elevation): 42848812.53769041 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 9.98e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.82e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 5.62e-06 ) ; ( Rwell ) = ( 2.04e-15 ) ; ( R ) = ( 5.62e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108185 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199782 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.52257e+07s, dt:6270.93s, Cycle: 731 +well_1Control: BHP (at the specified reference elevation): 42852769.12535773 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 5.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-04 ) ; ( Rwell ) = ( 8.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 7.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 6.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00540839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000999109 +Time: 4.5232e+07s, dt:6270.93s, Cycle: 732 +well_1Control: BHP (at the specified reference elevation): 42854743.69600177 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 6.72e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 8.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.11e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 8.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 9.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00540623 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000999192 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.52382e+07s, dt:12541.9s, Cycle: 733 +well_1Control: BHP (at the specified reference elevation): 42856715.85592233 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 9.96e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 8.79e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.95e-05 ) ; ( Rwell ) = ( 2.53e-15 ) ; ( R ) = ( 1.95e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199817 +Time: 4.52508e+07s, dt:12541.9s, Cycle: 734 +well_1Control: BHP (at the specified reference elevation): 42860668.52205224 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.95e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 8.07e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 7.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.63e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.38e-05 ) ; ( Rwell ) = ( 5.84e-16 ) ; ( R ) = ( 1.38e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00199859 +Time: 4.52633e+07s, dt:12541.9s, Cycle: 735 +well_1Control: BHP (at the specified reference elevation): 42864617.60862513 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 9.80e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.65e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 8.91e-16 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00200061 +Time: 4.52759e+07s, dt:12541.9s, Cycle: 736 +well_1Control: BHP (at the specified reference elevation): 42868566.20346394 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 1.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 9.65e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.97e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.13e-05 ) ; ( Rwell ) = ( 4.65e-15 ) ; ( R ) = ( 2.13e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.31e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 42872515.18064573 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0108099 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00200167 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.52884e+07s, dt:6270.93s, Cycle: 737 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 5.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-04 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.74e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 9.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00540428 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00100109 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.52947e+07s, dt:12541.9s, Cycle: 738 +well_1Control: BHP (at the specified reference elevation): 42874488.03242704 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.57e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 9.94e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 8.80e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.75e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.36e-05 ) ; ( Rwell ) = ( 7.67e-15 ) ; ( R ) = ( 2.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108098 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020015 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.53072e+07s, dt:25083.7s, Cycle: 739 +well_1Control: BHP (at the specified reference elevation): 42878435.403868295 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 2.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 1.46e-10 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 8.22e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 6.30e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.58e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.91e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.32e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.80e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.59e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.28e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.88e-05 ) ; ( Rwell ) = ( 1.42e-14 ) ; ( R ) = ( 2.88e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0216106 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00399638 +Time: 4.53323e+07s, dt:25083.7s, Cycle: 740 +well_1Control: BHP (at the specified reference elevation): 42886331.52059917 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 2.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.47e-10 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.22e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.14e-05 ) ; ( Rwell ) = ( 1.29e-14 ) ; ( R ) = ( 3.14e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0216034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00398282 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.53574e+07s, dt:50167.4s, Cycle: 741 +well_1Control: BHP (at the specified reference elevation): 42894228.63724209 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 5.80e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.39e-03 ) ; ( Rwell ) = ( 3.28e-10 ) ; ( R ) = ( 7.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 2.53e-10 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.23e-03 ) ; ( Rwell ) = ( 2.21e-10 ) ; ( R ) = ( 6.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 5.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 1.17e-10 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 9.04e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.13e-05 ) ; ( Rwell ) = ( 1.02e-13 ) ; ( R ) = ( 3.13e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0431882 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00787568 +Time: 4.54076e+07s, dt:50167.4s, Cycle: 742 +well_1Control: BHP (at the specified reference elevation): 42910008.65922329 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 6.07e-09 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.55e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 8.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 7.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 6.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 6.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 5.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 7.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.85e-05 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 3.85e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0431602 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00792699 +Time: 4.54577e+07s, dt:50167.4s, Cycle: 743 +well_1Control: BHP (at the specified reference elevation): 42925783.8653133 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 4.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 5.74e-10 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.72e-03 ) ; ( Rwell ) = ( 3.24e-10 ) ; ( R ) = ( 7.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.49e-10 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.50e-05 ) ; ( Rwell ) = ( 1.49e-13 ) ; ( R ) = ( 4.50e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0431323 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00797622 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.55079e+07s, dt:100335s, Cycle: 744 +well_1Control: BHP (at the specified reference elevation): 42941553.30878842 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.84e-10 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 1.94e-14 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0861888 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0159278 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.56082e+07s, dt:200670s, Cycle: 745 +well_1Control: BHP (at the specified reference elevation): 42973009.55982429 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.06e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 6.64e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.35e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 3.04e-09 ) ; ( R ) = ( 3.29e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 3.08e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 1.02e-12 ) ; ( R ) = ( 8.38e-04 ) ; + Last LinSolve(iter,res) = ( 11, 8.08e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 43035637.59227787 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.172006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.031518 +Time: 4.58089e+07s, dt:191099s, Cycle: 746 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.06e-08 ) ; ( R ) = ( 1.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 2.59e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 9.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 7.64e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 7.57e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 7.39e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 7.09e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 9.81e-10 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 6.78e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 8.62e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 6.49e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 7.60e-10 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 6.18e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 6.67e-10 ) ; ( R ) = ( 1.32e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.64e-04 ) ; ( Rwell ) = ( 3.24e-13 ) ; ( R ) = ( 3.64e-04 ) ; + Last LinSolve(iter,res) = ( 11, 6.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.163313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0295472 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.6e+07s, dt:95549.6s, Cycle: 747 +well_1Control: BHP (at the specified reference elevation): 43095273.630369924 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.43e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.52e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 8.93e-10 ) ; ( R ) = ( 9.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.84e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 7.86e-10 ) ; ( R ) = ( 6.30e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.64e-04 ) ; ( Rwell ) = ( 2.83e-13 ) ; ( R ) = ( 2.64e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0814785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0150029 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.49376e+07, 2.4978e+07, 2.50868e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.24175e+07, 1.25667e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.805 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 19.0381, 718.767 } rm^3 +compflowStatistics, reservoir: Phase mass: { 11645.5, 700629 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1693.88, 215814 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 9951.65, 484816 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 17.5251, 5.63115 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 11628, 700624 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 11645.5, 0 }, { 1983.55, 698597 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.47173e+07, 2.48736e+07, 2.49562e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.21971e+07, 1.24362e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.401 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.401 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219563 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65868.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153694 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219563 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27511e-08, 219563 } } kg +well_1Control: BHP (at the specified reference elevation): 43125140.77448331 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 197.539 +compflowStatistics: Max component CFL number: 271.467 +Time: 4.60955e+07s, dt:191099s, Cycle: 748 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 1.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.61e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 8.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; ( R ) = ( 3.22e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 3.51e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 1.41e-13 ) ; ( R ) = ( 4.98e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.162644 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.029872 +Time: 4.62866e+07s, dt:191099s, Cycle: 749 +well_1Control: BHP (at the specified reference elevation): 43184568.40978661 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 3.26e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 9.72e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.92e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 2.97e-10 ) ; ( R ) = ( 8.87e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.58e-04 ) ; ( Rwell ) = ( 7.14e-14 ) ; ( R ) = ( 2.58e-04 ) ; + Last LinSolve(iter,res) = ( 12, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.162205 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0293786 +Time: 4.64777e+07s, dt:191099s, Cycle: 750 +well_1Control: BHP (at the specified reference elevation): 43243934.64035838 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.72e-04 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 3.72e-04 ) ; + Last LinSolve(iter,res) = ( 11, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.161791 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.028996 +Time: 4.66688e+07s, dt:191099s, Cycle: 751 +well_1Control: BHP (at the specified reference elevation): 43303265.83786872 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 1.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 7.91e-09 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 9.97e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 9.55e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 9.11e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 8.71e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 9.55e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 8.30e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 8.40e-10 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 7.90e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 6.44e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 7.07e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 5.67e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 6.71e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.98e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 6.36e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.88e-05 ) ; ( Rwell ) = ( 1.46e-13 ) ; ( R ) = ( 3.88e-05 ) ; + Last LinSolve(iter,res) = ( 10, 9.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.161404 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0283676 +Time: 4.68599e+07s, dt:140054s, Cycle: 752 +well_1Control: BHP (at the specified reference elevation): 43362524.681023076 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.22e-03 ) ; ( Rwell ) = ( 4.26e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 3.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.68e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.56e-03 ) ; ( Rwell ) = ( 3.35e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 3.90e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 3.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.59e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 3.08e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.57e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.88e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.83e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 3.28e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 2.47e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.43e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.61e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 3.01e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.11e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.35e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.40e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.76e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 1.83e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.26e-10 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.73e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 1.58e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.78e-05 ) ; ( Rwell ) = ( 9.76e-14 ) ; ( R ) = ( 7.78e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.118051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0207249 +Time: 4.7e+07s, dt:140054s, Cycle: 753 +well_1Control: BHP (at the specified reference elevation): 43405996.56008267 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.86e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.82e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 9.97e-09 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.40e-04 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.40e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117879 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.020735 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.51561e+07, 2.51965e+07, 2.53054e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.26268e+07, 1.2776e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 737.964 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 19.3651, 718.599 } rm^3 +compflowStatistics, reservoir: Phase mass: { 11916.7, 700586 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1731.71, 215898 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 10185, 484687 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 18.6498, 5.70116 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 11898, 700580 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 11916.7, 0 }, { 2021.26, 698514 } } kg +well_1Control: BHP (at the specified reference elevation): 43449433.0942537 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.49366e+07, 2.50922e+07, 2.51747e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.24072e+07, 1.26454e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.45 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.45 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219646 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65893.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153752 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219646 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27597e-08, 219646 } } kg +compflowStatistics: Max phase CFL number: 287.774 +compflowStatistics: Max component CFL number: 395.475 +Time: 4.71401e+07s, dt:70026.9s, Cycle: 754 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.20e-03 ) ; ( Rwell ) = ( 6.06e-10 ) ; ( R ) = ( 7.20e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 4.70e-10 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 4.13e-10 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.63e-10 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.91e-05 ) ; ( Rwell ) = ( 3.64e-15 ) ; ( R ) = ( 6.91e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0588649 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0102798 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.72101e+07s, dt:140054s, Cycle: 755 +well_1Control: BHP (at the specified reference elevation): 43471174.80043501 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 4.27e-09 ) ; ( R ) = ( 3.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.86e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 9.27e-10 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 5.21e-10 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 1.33e-10 ) ; ( R ) = ( 7.44e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.72e-05 ) ; ( Rwell ) = ( 1.49e-14 ) ; ( R ) = ( 6.72e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0207659 +Time: 4.73501e+07s, dt:140054s, Cycle: 756 +well_1Control: BHP (at the specified reference elevation): 43514503.97151621 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.75e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.21e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.94e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 9.28e-10 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 8.12e-10 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 2.06e-10 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.89e-05 ) ; ( Rwell ) = ( 2.81e-14 ) ; ( R ) = ( 8.89e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0208387 +Time: 4.74902e+07s, dt:140054s, Cycle: 757 +well_1Control: BHP (at the specified reference elevation): 43557797.02071207 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.56e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 4.15e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 4.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.42e-03 ) ; ( Rwell ) = ( 1.45e-08 ) ; ( R ) = ( 9.42e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.17e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.17e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0212251 +Time: 4.76302e+07s, dt:140054s, Cycle: 758 +well_1Control: BHP (at the specified reference elevation): 43601040.25011616 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 1.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 9.19e-10 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 8.09e-10 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 7.09e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 1.79e-10 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.73e-05 ) ; ( Rwell ) = ( 2.83e-14 ) ; ( R ) = ( 5.73e-05 ) ; + Last LinSolve(iter,res) = ( 10, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117147 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.021177 +Time: 4.77703e+07s, dt:140054s, Cycle: 759 +well_1Control: BHP (at the specified reference elevation): 43644188.08971774 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 1.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 8.97e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 6.07e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 7.69e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 8.37e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 9.26e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.87e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.70e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 7.18e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 7.81e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 8.15e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-04 ) ; ( Rwell ) = ( 1.51e-13 ) ; ( R ) = ( 1.04e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.116966 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0208939 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.79103e+07s, dt:89650.3s, Cycle: 760 +well_1Control: BHP (at the specified reference elevation): 43687271.81180751 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.97e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.66e-03 ) ; ( Rwell ) = ( 4.36e-10 ) ; ( R ) = ( 9.66e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 3.83e-10 ) ; ( R ) = ( 7.77e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 3.37e-10 ) ; ( R ) = ( 7.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 2.96e-10 ) ; ( R ) = ( 7.19e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.44e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.55e-03 ) ; ( Rwell ) = ( 2.61e-10 ) ; ( R ) = ( 8.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.47e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.93e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.16e-03 ) ; ( Rwell ) = ( 2.29e-10 ) ; ( R ) = ( 8.16e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.93e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.63e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.50e-03 ) ; ( Rwell ) = ( 2.02e-10 ) ; ( R ) = ( 7.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.74e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 1.77e-10 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 1.56e-10 ) ; ( R ) = ( 6.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.12e-05 ) ; ( Rwell ) = ( 1.14e-14 ) ; ( R ) = ( 6.12e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0747676 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0132508 +Time: 4.8e+07s, dt:89650.3s, Cycle: 761 +well_1Control: BHP (at the specified reference elevation): 43714862.647693574 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 8.40e-09 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.72e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 7.20e-09 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.75e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 7.16e-09 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.37e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 7.11e-09 ) ; ( R ) = ( 8.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.94e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; ( R ) = ( 8.35e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.10e-05 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 9.10e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.76e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 43742446.03434862 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0746941 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0134282 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.53546e+07, 2.5395e+07, 2.5504e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.28359e+07, 1.29852e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 738.108 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 19.6633, 718.445 } rm^3 +compflowStatistics, reservoir: Phase mass: { 12164.6, 700544 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1765.46, 215975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 10399.1, 484569 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 18.0962, 6.18467 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 12146.5, 700538 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 12164.6, 0 }, { 2054.09, 698439 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.51355e+07, 2.52909e+07, 2.53732e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.26167e+07, 1.28545e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.494 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.494 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219721 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65916.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153804 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219721 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27674e-08, 219721 } } kg +compflowStatistics: Max phase CFL number: 183.205 +compflowStatistics: Max component CFL number: 251.772 +Time: 4.80897e+07s, dt:179301s, Cycle: 762 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 1.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 6.69e-09 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; ( R ) = ( 6.48e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 2.77e-13 ) ; ( R ) = ( 4.06e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.149182 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0262418 +Time: 4.8269e+07s, dt:179301s, Cycle: 763 +well_1Control: BHP (at the specified reference elevation): 43797314.94238711 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 9.92e-09 ) ; ( R ) = ( 1.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; ( R ) = ( 5.71e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 9.98e-10 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 8.77e-10 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 7.72e-10 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 6.79e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.40e-04 ) ; ( Rwell ) = ( 2.76e-13 ) ; ( R ) = ( 2.40e-04 ) ; + Last LinSolve(iter,res) = ( 10, 7.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.148841 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0260239 +Time: 4.84483e+07s, dt:179301s, Cycle: 764 +well_1Control: BHP (at the specified reference elevation): 43852121.19099548 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 9.88e-09 ) ; ( R ) = ( 1.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 4.54e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 7.80e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 9.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 9.47e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 9.19e-10 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 8.08e-10 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 7.11e-10 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 1.44e-13 ) ; ( R ) = ( 4.36e-04 ) ; + Last LinSolve(iter,res) = ( 10, 7.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.148507 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0259989 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.86276e+07s, dt:89650.3s, Cycle: 765 +well_1Control: BHP (at the specified reference elevation): 43906925.03970252 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.76e-03 ) ; ( Rwell ) = ( 9.86e-09 ) ; ( R ) = ( 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.80e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 9.54e-10 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 7.32e-10 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 6.43e-10 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.25e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.65e-10 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.39e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.98e-10 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.33e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 3.85e-10 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.10e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.71e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 3.39e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.92e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.72e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.94e-03 ) ; ( Rwell ) = ( 2.97e-10 ) ; ( R ) = ( 9.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.83e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.00e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 2.61e-10 ) ; ( R ) = ( 9.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.70e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.97e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.93e-03 ) ; ( Rwell ) = ( 2.30e-10 ) ; ( R ) = ( 7.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.87e-05 ) ; ( Rwell ) = ( 6.87e-14 ) ; ( R ) = ( 5.87e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0741214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.01293 +Time: 4.87172e+07s, dt:89650.3s, Cycle: 766 +well_1Control: BHP (at the specified reference elevation): 43934373.5881065 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.76e-03 ) ; ( Rwell ) = ( 9.85e-09 ) ; ( R ) = ( 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 7.11e-09 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 5.91e-09 ) ; ( R ) = ( 1.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.45e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 8.45e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.29e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.10e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 8.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.50e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 7.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.91e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.52e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 6.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.64e-05 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 4.64e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.17e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 43961799.13556478 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0740479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0128511 +Time: 4.88069e+07s, dt:89650.3s, Cycle: 767 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.67e-03 ) ; ( Rwell ) = ( 9.83e-09 ) ; ( R ) = ( 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.86e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 9.38e-10 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.59e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 7.27e-10 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.92e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 6.37e-10 ) ; ( R ) = ( 9.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 5.60e-10 ) ; ( R ) = ( 8.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.66e-03 ) ; ( Rwell ) = ( 4.93e-10 ) ; ( R ) = ( 7.66e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 4.34e-10 ) ; ( R ) = ( 7.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.40e-03 ) ; ( Rwell ) = ( 3.82e-10 ) ; ( R ) = ( 7.40e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 3.36e-10 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.31e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 2.95e-10 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.42e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.73e-05 ) ; ( Rwell ) = ( 1.84e-14 ) ; ( R ) = ( 2.73e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0739799 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0131327 +Time: 4.88965e+07s, dt:89650.3s, Cycle: 768 +well_1Control: BHP (at the specified reference elevation): 43989180.73177676 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.83e-03 ) ; ( Rwell ) = ( 9.80e-09 ) ; ( R ) = ( 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 9.40e-10 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.94e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 5.33e-10 ) ; ( R ) = ( 9.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.28e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 4.09e-10 ) ; ( R ) = ( 9.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.45e-03 ) ; ( Rwell ) = ( 3.60e-10 ) ; ( R ) = ( 9.45e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 3.17e-10 ) ; ( R ) = ( 8.98e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.05e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 2.78e-10 ) ; ( R ) = ( 7.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 2.44e-10 ) ; ( R ) = ( 7.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.89e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 2.15e-10 ) ; ( R ) = ( 7.45e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.77e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.89e-03 ) ; ( Rwell ) = ( 1.89e-10 ) ; ( R ) = ( 6.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.74e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 1.66e-10 ) ; ( R ) = ( 6.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.74e-05 ) ; ( Rwell ) = ( 1.66e-13 ) ; ( R ) = ( 6.74e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0739123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0132123 +Time: 4.89862e+07s, dt:13846.4s, Cycle: 769 +well_1Control: BHP (at the specified reference elevation): 44016527.475614496 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.77e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 7.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 8.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 9.63e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.46e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.61e-05 ) ; ( Rwell ) = ( 2.61e-15 ) ; ( R ) = ( 2.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114068 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204722 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.9e+07s, dt:6923.21s, Cycle: 770 +well_1Control: BHP (at the specified reference elevation): 44020760.97438551 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 9.79e-09 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 5.49e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00570221 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102546 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +well_1Control: BHP (at the specified reference elevation): 44022874.46519363 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.55455e+07, 2.55859e+07, 2.5695e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.3044e+07, 1.31935e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 738.247 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 19.9495, 718.297 } rm^3 +compflowStatistics, reservoir: Phase mass: { 12403.5, 700505 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1798.09, 216049 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 10605.4, 484457 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 18.4553, 6.18546 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 12385.1, 700499 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 12403.5, 0 }, { 2086.39, 698367 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.5327e+07, 2.54819e+07, 2.55641e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.28256e+07, 1.30627e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.536 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.536 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219793 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65937.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153855 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219793 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27749e-08, 219793 } } kg +compflowStatistics: Max phase CFL number: 14.0753 +compflowStatistics: Max component CFL number: 19.3432 +Time: 4.90069e+07s, dt:13846.4s, Cycle: 771 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.77e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 4.02e-11 ) ; ( R ) = ( 6.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 9.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 3.54e-11 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 9.36e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 7.48e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 6.62e-16 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205593 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.90208e+07s, dt:6923.21s, Cycle: 772 +well_1Control: BHP (at the specified reference elevation): 44027106.45409316 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 9.79e-09 ) ; ( R ) = ( 6.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 5.19e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00570084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102929 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.90277e+07s, dt:13846.4s, Cycle: 773 +well_1Control: BHP (at the specified reference elevation): 44029219.730427735 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.76e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.02e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; ( R ) = ( 7.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 6.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 8.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 7.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.85e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 5.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.56e-05 ) ; ( Rwell ) = ( 8.73e-16 ) ; ( R ) = ( 2.56e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206209 +Time: 4.90415e+07s, dt:13846.4s, Cycle: 774 +well_1Control: BHP (at the specified reference elevation): 44033452.87740239 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.79e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.90e-03 ) ; ( Rwell ) = ( 4.01e-11 ) ; ( R ) = ( 6.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.85e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 5.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 5.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 8.69e-12 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.43e-05 ) ; ( Rwell ) = ( 5.96e-15 ) ; ( R ) = ( 2.43e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206471 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.90554e+07s, dt:6923.21s, Cycle: 775 +well_1Control: BHP (at the specified reference elevation): 44037687.38644147 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 9.79e-09 ) ; ( R ) = ( 6.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 8.47e-12 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 8.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 6.75e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 5.62e-12 ) ; ( R ) = ( 4.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00569935 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103301 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.90623e+07s, dt:13846.4s, Cycle: 776 +well_1Control: BHP (at the specified reference elevation): 44039801.97876475 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.77e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 4.04e-11 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 3.56e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 8.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 9.20e-12 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 7.95e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 7.03e-12 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 6.18e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.16e-05 ) ; ( Rwell ) = ( 2.66e-15 ) ; ( R ) = ( 2.16e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.43e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44044035.84772022 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206688 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.90762e+07s, dt:6923.21s, Cycle: 777 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 9.79e-09 ) ; ( R ) = ( 6.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.41e-11 ) ; ( R ) = ( 6.07e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00570359 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103347 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.90831e+07s, dt:13846.4s, Cycle: 778 +well_1Control: BHP (at the specified reference elevation): 44046147.43063709 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.75e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.20e-03 ) ; ( Rwell ) = ( 4.23e-11 ) ; ( R ) = ( 9.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.26e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 8.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 2.90e-11 ) ; ( R ) = ( 7.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 7.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 7.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 6.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 5.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 9.74e-12 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 8.66e-12 ) ; ( R ) = ( 4.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 6.85e-12 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.98e-05 ) ; ( Rwell ) = ( 2.52e-15 ) ; ( R ) = ( 1.98e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114019 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206645 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.90969e+07s, dt:6923.21s, Cycle: 779 +well_1Control: BHP (at the specified reference elevation): 44050370.639641285 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 9.72e-09 ) ; ( R ) = ( 6.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.23e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00569636 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103286 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.91038e+07s, dt:13846.4s, Cycle: 780 +well_1Control: BHP (at the specified reference elevation): 44052474.27252786 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.69e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 4.13e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 6.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 9.98e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 8.80e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.39e-05 ) ; ( Rwell ) = ( 2.96e-15 ) ; ( R ) = ( 1.39e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44056705.78638611 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113968 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206372 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.91177e+07s, dt:6923.21s, Cycle: 781 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 9.75e-09 ) ; ( R ) = ( 6.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 5.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00569543 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103154 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.91246e+07s, dt:13846.4s, Cycle: 782 +well_1Control: BHP (at the specified reference elevation): 44058817.41942255 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.72e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 3.94e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 3.01e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 7.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 6.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 9.08e-12 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.71e-05 ) ; ( Rwell ) = ( 9.70e-16 ) ; ( R ) = ( 3.71e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44063044.17863193 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113934 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205999 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.91385e+07s, dt:6923.21s, Cycle: 783 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 6.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00569399 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010293 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.91454e+07s, dt:13846.4s, Cycle: 784 +well_1Control: BHP (at the specified reference elevation): 44065155.41925564 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.72e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.44e-03 ) ; ( Rwell ) = ( 4.02e-11 ) ; ( R ) = ( 6.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 3.17e-11 ) ; ( R ) = ( 6.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 2.80e-11 ) ; ( R ) = ( 6.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 7.91e-12 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 7.59e-16 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113915 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205406 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.91592e+07s, dt:6923.21s, Cycle: 785 +well_1Control: BHP (at the specified reference elevation): 44069381.77057128 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 6.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 5.38e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00569291 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102595 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.91662e+07s, dt:13846.4s, Cycle: 786 +well_1Control: BHP (at the specified reference elevation): 44071492.27258315 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.72e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.57e-03 ) ; ( Rwell ) = ( 4.05e-11 ) ; ( R ) = ( 7.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 3.56e-11 ) ; ( R ) = ( 7.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 2.77e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 2.45e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.54e-05 ) ; ( Rwell ) = ( 8.00e-15 ) ; ( R ) = ( 1.54e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113891 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204676 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.918e+07s, dt:6923.21s, Cycle: 787 +well_1Control: BHP (at the specified reference elevation): 44075718.06047528 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 6.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-04 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 4.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44077824.10325208 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00569177 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102243 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.91869e+07s, dt:13846.4s, Cycle: 788 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 4.09e-11 ) ; ( R ) = ( 5.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 6.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 6.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 5.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 5.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.25e-05 ) ; ( Rwell ) = ( 2.26e-15 ) ; ( R ) = ( 2.25e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113873 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00203852 +Time: 4.92008e+07s, dt:13846.4s, Cycle: 789 +well_1Control: BHP (at the specified reference elevation): 44082052.3728272 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 4.07e-11 ) ; ( R ) = ( 6.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 5.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 3.79e-15 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.19e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44086277.902026296 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113824 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204593 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.92146e+07s, dt:6923.21s, Cycle: 790 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 6.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 5.49e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44088387.70381164 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00568974 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102486 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.92215e+07s, dt:13846.4s, Cycle: 791 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.71e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 8.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 7.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 4.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 8.10e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.62e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; +New dt = 6923.209744691849 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 9.71e-09 ) ; ( R ) = ( 6.13e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 5.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0056878 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102629 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 6923.209744691849, remaining dt = 6923.209744691849 +well_1Control: BHP (at the specified reference elevation): 44090491.886944056 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 6.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00570111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102765 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.92354e+07s, dt:13846.4s, Cycle: 792 +well_1Control: BHP (at the specified reference elevation): 44092599.515206724 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 4.11e-11 ) ; ( R ) = ( 8.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 7.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 3.19e-11 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 6.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.13e-06 ) ; ( Rwell ) = ( 1.17e-15 ) ; ( R ) = ( 9.13e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.011382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205957 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.92492e+07s, dt:6923.21s, Cycle: 793 +well_1Control: BHP (at the specified reference elevation): 44096825.151662424 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 6.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 9.95e-12 ) ; ( R ) = ( 5.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44098933.667004794 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00568773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103089 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.92562e+07s, dt:13846.4s, Cycle: 794 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 4.11e-11 ) ; ( R ) = ( 7.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 7.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.77e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 2.44e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.43e-05 ) ; ( Rwell ) = ( 7.60e-15 ) ; ( R ) = ( 3.43e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113806 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206513 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.927e+07s, dt:6923.21s, Cycle: 795 +well_1Control: BHP (at the specified reference elevation): 44103157.35354737 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 6.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 5.21e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44105265.26109856 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00568686 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103355 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.92769e+07s, dt:13846.4s, Cycle: 796 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.61e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 3.94e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 3.02e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 2.66e-11 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 9.48e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 8.35e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 7.28e-12 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.61e-05 ) ; ( Rwell ) = ( 2.47e-15 ) ; ( R ) = ( 2.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.43e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44109491.57240522 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113777 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206789 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.92908e+07s, dt:6923.21s, Cycle: 797 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 6.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 9.77e-12 ) ; ( R ) = ( 5.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00568504 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103425 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.92977e+07s, dt:13846.4s, Cycle: 798 +well_1Control: BHP (at the specified reference elevation): 44111601.2513524 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.71e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 6.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 7.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 9.08e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 7.12e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.64e-05 ) ; ( Rwell ) = ( 7.45e-15 ) ; ( R ) = ( 3.64e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113778 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206972 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.93115e+07s, dt:6923.21s, Cycle: 799 +well_1Control: BHP (at the specified reference elevation): 44115825.57790555 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 5.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00568379 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103526 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.93185e+07s, dt:13846.4s, Cycle: 800 +well_1Control: BHP (at the specified reference elevation): 44117934.063289754 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.70e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 9.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 9.81e-12 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 8.64e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 7.62e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.85e-05 ) ; ( Rwell ) = ( 4.04e-15 ) ; ( R ) = ( 3.85e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113754 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00207165 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.93323e+07s, dt:6923.21s, Cycle: 801 +well_1Control: BHP (at the specified reference elevation): 44122153.18755409 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 9.69e-09 ) ; ( R ) = ( 6.22e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 5.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.005689 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103642 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.93392e+07s, dt:13846.4s, Cycle: 802 +well_1Control: BHP (at the specified reference elevation): 44124257.63731672 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 9.91e-12 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 7.89e-12 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 6.18e-12 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.31e-12 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; +New dt = 6923.209744691849 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 6.22e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 5.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44126360.466471314 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00571213 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103676 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 6923.209744691849, remaining dt = 6923.209744691849 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 9.65e-09 ) ; ( R ) = ( 6.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 5.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00571783 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103633 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.93531e+07s, dt:13846.4s, Cycle: 803 +well_1Control: BHP (at the specified reference elevation): 44128464.84712793 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; ( R ) = ( 1.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 4.03e-11 ) ; ( R ) = ( 7.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 9.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 3.55e-11 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 6.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 6.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 2.45e-11 ) ; ( R ) = ( 6.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 4.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 9.83e-12 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 8.96e-12 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.60e-12 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.12e-05 ) ; ( Rwell ) = ( 3.68e-15 ) ; ( R ) = ( 3.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113722 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00207001 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.93669e+07s, dt:6923.21s, Cycle: 804 +well_1Control: BHP (at the specified reference elevation): 44132682.42848498 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 6.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.24e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44134788.692198634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00568239 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103452 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.93739e+07s, dt:13846.4s, Cycle: 805 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 4.04e-11 ) ; ( R ) = ( 7.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 3.56e-11 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 5.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.77e-11 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 2.44e-11 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 8.09e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.54e-05 ) ; ( Rwell ) = ( 9.15e-15 ) ; ( R ) = ( 2.54e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113684 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206571 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.93877e+07s, dt:6923.21s, Cycle: 806 +well_1Control: BHP (at the specified reference elevation): 44139006.4667947 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 6.22e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00568085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103214 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.93946e+07s, dt:13846.4s, Cycle: 807 +well_1Control: BHP (at the specified reference elevation): 44141112.94661247 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-03 ) ; ( Rwell ) = ( 4.08e-11 ) ; ( R ) = ( 5.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 2.77e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 7.65e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 6.76e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.26e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.35e-05 ) ; ( Rwell ) = ( 2.91e-15 ) ; ( R ) = ( 1.35e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.26e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44145329.6083062 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113665 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205919 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.94085e+07s, dt:6923.21s, Cycle: 808 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 8.01e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00568059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102807 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.94154e+07s, dt:13846.4s, Cycle: 809 +well_1Control: BHP (at the specified reference elevation): 44147429.27101526 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.59e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 7.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 9.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 3.58e-11 ) ; ( R ) = ( 7.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 8.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 3.18e-11 ) ; ( R ) = ( 6.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 6.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 9.14e-12 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 8.09e-12 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.75e-05 ) ; ( Rwell ) = ( 2.68e-15 ) ; ( R ) = ( 4.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113656 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020496 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.94292e+07s, dt:6923.21s, Cycle: 810 +well_1Control: BHP (at the specified reference elevation): 44151649.04688524 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 9.69e-09 ) ; ( R ) = ( 6.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 9.96e-12 ) ; ( R ) = ( 5.42e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00567856 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102324 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.94362e+07s, dt:13846.4s, Cycle: 811 +well_1Control: BHP (at the specified reference elevation): 44153755.83568055 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 8.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 8.96e-12 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.92e-12 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 6.22e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.23e-05 ) ; ( Rwell ) = ( 9.78e-16 ) ; ( R ) = ( 2.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113611 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204483 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.945e+07s, dt:6923.21s, Cycle: 812 +well_1Control: BHP (at the specified reference elevation): 44157972.1106196 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 6.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 6.23e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44160076.000038534 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00567877 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102288 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.94569e+07s, dt:13846.4s, Cycle: 813 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.64e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.09e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 9.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 3.41e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 7.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 8.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 9.77e-12 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204637 +Time: 4.94708e+07s, dt:13846.4s, Cycle: 814 +well_1Control: BHP (at the specified reference elevation): 44164287.38290648 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 3.89e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 7.64e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.12e-05 ) ; ( Rwell ) = ( 4.34e-15 ) ; ( R ) = ( 3.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.99e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44168504.21953273 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204592 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.94846e+07s, dt:6923.21s, Cycle: 815 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 6.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00567667 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102276 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.94915e+07s, dt:13846.4s, Cycle: 816 +well_1Control: BHP (at the specified reference elevation): 44170606.88614742 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.64e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 3.96e-11 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 3.49e-11 ) ; ( R ) = ( 6.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 8.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 5.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 4.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 9.69e-12 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 8.54e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.52e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.63e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.24e-05 ) ; ( Rwell ) = ( 1.21e-15 ) ; ( R ) = ( 3.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113544 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204345 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.95054e+07s, dt:6923.21s, Cycle: 817 +well_1Control: BHP (at the specified reference elevation): 44174822.39160296 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 9.67e-09 ) ; ( R ) = ( 6.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 4.74e-10 ) ; ( R ) = ( 4.67e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00567463 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102136 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.95123e+07s, dt:13846.4s, Cycle: 818 +well_1Control: BHP (at the specified reference elevation): 44176924.573294245 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.17e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 3.96e-11 ) ; ( R ) = ( 6.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 8.99e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 9.06e-16 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00203887 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.95262e+07s, dt:6923.21s, Cycle: 819 +well_1Control: BHP (at the specified reference elevation): 44181136.32441659 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 6.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.09e-04 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 5.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44183238.09047735 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00567397 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101863 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.95331e+07s, dt:13846.4s, Cycle: 820 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.63e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 4.01e-11 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 2.72e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 9.42e-12 ) ; ( R ) = ( 5.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00203232 +Time: 4.95469e+07s, dt:13846.4s, Cycle: 821 +well_1Control: BHP (at the specified reference elevation): 44187447.347982466 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.65e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 3.89e-11 ) ; ( R ) = ( 5.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 7.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 8.44e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 3.10e-11 ) ; ( R ) = ( 7.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 7.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 6.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 6.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 5.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 5.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 1.10e-14 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00203125 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.95608e+07s, dt:6923.21s, Cycle: 822 +well_1Control: BHP (at the specified reference elevation): 44191659.85534263 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 9.65e-09 ) ; ( R ) = ( 6.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 4.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00567272 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101776 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.95677e+07s, dt:13846.4s, Cycle: 823 +well_1Control: BHP (at the specified reference elevation): 44193760.36925723 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.96e-05 ) ; ( Rwell ) = ( 2.89e-15 ) ; ( R ) = ( 2.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204266 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.95815e+07s, dt:6923.21s, Cycle: 824 +well_1Control: BHP (at the specified reference elevation): 44197966.62248299 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 9.62e-09 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-04 ) ; ( Rwell ) = ( 9.94e-12 ) ; ( R ) = ( 4.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00567057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102333 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.95885e+07s, dt:13846.4s, Cycle: 825 +well_1Control: BHP (at the specified reference elevation): 44200066.71014282 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 3.92e-11 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 3.01e-11 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.65e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 9.35e-12 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 8.22e-12 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.34e-05 ) ; ( Rwell ) = ( 4.09e-15 ) ; ( R ) = ( 4.34e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205188 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.96023e+07s, dt:6923.21s, Cycle: 826 +well_1Control: BHP (at the specified reference elevation): 44204270.97613165 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 6.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 5.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00566957 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102726 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.96092e+07s, dt:13846.4s, Cycle: 827 +well_1Control: BHP (at the specified reference elevation): 44206370.541918784 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 3.92e-11 ) ; ( R ) = ( 6.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 6.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 2.37e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 4.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 9.64e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 8.33e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.05e-05 ) ; ( Rwell ) = ( 5.66e-15 ) ; ( R ) = ( 3.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44210574.42311762 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205858 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.96231e+07s, dt:6923.21s, Cycle: 828 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 6.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00566893 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103057 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.963e+07s, dt:13846.4s, Cycle: 829 +well_1Control: BHP (at the specified reference elevation): 44212673.853521034 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.59e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 2.28e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 4.04e-05 ) ; ( Rwell ) = ( 4.10e-15 ) ; ( R ) = ( 4.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113408 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206296 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.96439e+07s, dt:6923.21s, Cycle: 830 +well_1Control: BHP (at the specified reference elevation): 44216877.513089076 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 6.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 5.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44218974.90045839 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0056675 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103217 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.96508e+07s, dt:13846.4s, Cycle: 831 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.69e-03 ) ; ( Rwell ) = ( 3.89e-11 ) ; ( R ) = ( 6.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 3.42e-11 ) ; ( R ) = ( 6.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 5.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 2.63e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 7.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 4.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 8.13e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.70e-05 ) ; ( Rwell ) = ( 3.74e-15 ) ; ( R ) = ( 1.70e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206509 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.96646e+07s, dt:6923.21s, Cycle: 832 +well_1Control: BHP (at the specified reference elevation): 44223178.436977655 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 6.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 4.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00566576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103324 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.96716e+07s, dt:13846.4s, Cycle: 833 +well_1Control: BHP (at the specified reference elevation): 44225275.039450996 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.58e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 3.96e-11 ) ; ( R ) = ( 6.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 5.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 9.71e-12 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 8.39e-12 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.64e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 5.98e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.40e-05 ) ; ( Rwell ) = ( 6.04e-15 ) ; ( R ) = ( 4.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206557 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.96854e+07s, dt:6923.21s, Cycle: 834 +well_1Control: BHP (at the specified reference elevation): 44229477.09221558 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 5.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44231572.93302103 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00566434 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103324 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.96923e+07s, dt:13846.4s, Cycle: 835 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 6.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.31e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 5.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.09e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 6923.209744691849 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 9.80e-12 ) ; ( R ) = ( 5.04e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00566005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103245 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 6923.209744691849, remaining dt = 6923.209744691849 +well_1Control: BHP (at the specified reference elevation): 44233667.447180435 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 9.96e-12 ) ; ( R ) = ( 4.77e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44235763.501717344 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00566264 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103223 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.97062e+07s, dt:13846.4s, Cycle: 836 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 8.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.89e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 7.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 6.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.49e-03 ) ; ( Rwell ) = ( 3.17e-11 ) ; ( R ) = ( 7.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 2.78e-11 ) ; ( R ) = ( 7.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 6.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 8.16e-12 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.93e-05 ) ; ( Rwell ) = ( 1.08e-14 ) ; ( R ) = ( 3.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113357 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00206132 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.972e+07s, dt:6923.21s, Cycle: 837 +well_1Control: BHP (at the specified reference elevation): 44239963.255224645 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 6.21e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.00e-04 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.00e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44242055.00742036 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00566312 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00103056 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.97269e+07s, dt:13846.4s, Cycle: 838 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 3.52e-11 ) ; ( R ) = ( 4.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.37e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.32e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.21e-05 ) ; ( Rwell ) = ( 2.86e-16 ) ; ( R ) = ( 1.21e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113344 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00205662 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.97408e+07s, dt:6923.21s, Cycle: 839 +well_1Control: BHP (at the specified reference elevation): 44246254.9163713 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 6.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 9.83e-12 ) ; ( R ) = ( 5.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44248350.78702311 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00566119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102745 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.97477e+07s, dt:13846.4s, Cycle: 840 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 7.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 8.38e-12 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 7.39e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.74e-12 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 4.10e-05 ) ; ( Rwell ) = ( 5.82e-15 ) ; ( R ) = ( 4.10e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113292 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00204969 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.97616e+07s, dt:6923.21s, Cycle: 841 +well_1Control: BHP (at the specified reference elevation): 44252550.60495201 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 6.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 9.57e-12 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 8.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.89e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.32e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.36e-04 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 3.36e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44254649.90743555 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00566088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102369 +Time: 4.97685e+07s, dt:6923.21s, Cycle: 842 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 9.59e-09 ) ; ( R ) = ( 6.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 7.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 7.79e-12 ) ; ( R ) = ( 5.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44256740.56391173 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0056587 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00102252 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.97754e+07s, dt:13846.4s, Cycle: 843 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 1.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 3.52e-11 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 4.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 8.94e-12 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 7.91e-12 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 6.99e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.29e-05 ) ; ( Rwell ) = ( 3.12e-16 ) ; ( R ) = ( 3.29e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00203561 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.97892e+07s, dt:6923.21s, Cycle: 844 +well_1Control: BHP (at the specified reference elevation): 44260944.203116715 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 6.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00565871 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101625 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.97962e+07s, dt:13846.4s, Cycle: 845 +well_1Control: BHP (at the specified reference elevation): 44263036.90098292 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.90e-03 ) ; ( Rwell ) = ( 3.96e-11 ) ; ( R ) = ( 7.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.09e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 7.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 2.69e-11 ) ; ( R ) = ( 7.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.27e-03 ) ; ( Rwell ) = ( 2.44e-11 ) ; ( R ) = ( 8.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 6.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 5.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 5.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 9.89e-12 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 7.71e-12 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.70e-05 ) ; ( Rwell ) = ( 3.51e-15 ) ; ( R ) = ( 1.70e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113233 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202458 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.981e+07s, dt:6923.21s, Cycle: 846 +well_1Control: BHP (at the specified reference elevation): 44267234.626089185 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 6.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 5.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44269328.61661658 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00565825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101067 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.98169e+07s, dt:13846.4s, Cycle: 847 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 1.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 3.53e-11 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 9.78e-12 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 8.59e-12 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 7.60e-12 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 5.91e-12 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.90e-05 ) ; ( Rwell ) = ( 1.02e-14 ) ; ( R ) = ( 4.90e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113191 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202177 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.98308e+07s, dt:6923.21s, Cycle: 848 +well_1Control: BHP (at the specified reference elevation): 44273523.034693465 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 6.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44275613.15402284 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00565721 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101138 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.98377e+07s, dt:13846.4s, Cycle: 849 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; ( R ) = ( 1.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 4.01e-11 ) ; ( R ) = ( 6.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 3.54e-11 ) ; ( R ) = ( 6.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.26e-05 ) ; ( Rwell ) = ( 1.79e-15 ) ; ( R ) = ( 1.26e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113166 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202332 +Time: 4.98516e+07s, dt:13846.4s, Cycle: 850 +well_1Control: BHP (at the specified reference elevation): 44279808.79886778 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 3.98e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 8.76e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 6.07e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; +New dt = 6923.209744691849 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 6.08e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 5.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00565578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101252 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 6923.209744691849, remaining dt = 6923.209744691849 +well_1Control: BHP (at the specified reference elevation): 44281900.25286701 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 9.52e-09 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 5.53e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00565178 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101325 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.98654e+07s, dt:13846.4s, Cycle: 851 +well_1Control: BHP (at the specified reference elevation): 44283989.85158424 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 7.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 8.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.50e-11 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 9.02e-12 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 7.99e-12 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; +New dt = 6923.209744691849 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 9.51e-09 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 9.83e-12 ) ; ( R ) = ( 5.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44286084.34235207 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00566709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101329 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 6923.209744691849, remaining dt = 6923.209744691849 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 5.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0056673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010133 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.98792e+07s, dt:13846.4s, Cycle: 852 +well_1Control: BHP (at the specified reference elevation): 44288178.63650459 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 3.97e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 8.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 2.35e-11 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 9.41e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 8.27e-12 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 7.28e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.64e-05 ) ; ( Rwell ) = ( 5.77e-16 ) ; ( R ) = ( 2.64e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020262 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.98931e+07s, dt:6923.21s, Cycle: 853 +well_1Control: BHP (at the specified reference elevation): 44292372.43932967 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 9.96e-12 ) ; ( R ) = ( 6.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44294466.65935819 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00565145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101272 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.99e+07s, dt:13846.4s, Cycle: 854 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 3.91e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.50e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 6.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 9.56e-12 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 8.46e-12 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.63e-12 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.47e-06 ) ; ( Rwell ) = ( 2.82e-15 ) ; ( R ) = ( 4.47e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44298657.124358654 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202467 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.99139e+07s, dt:6923.21s, Cycle: 855 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 6.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 9.56e-12 ) ; ( R ) = ( 5.31e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00565069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101223 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.99208e+07s, dt:13846.4s, Cycle: 856 +well_1Control: BHP (at the specified reference elevation): 44300748.64867057 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.24e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 8.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.33e-03 ) ; ( Rwell ) = ( 3.54e-11 ) ; ( R ) = ( 7.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 8.09e-12 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.14e-05 ) ; ( Rwell ) = ( 2.19e-15 ) ; ( R ) = ( 3.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0020239 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.99346e+07s, dt:6923.21s, Cycle: 857 +well_1Control: BHP (at the specified reference elevation): 44304941.390976876 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 5.35e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00564979 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101203 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.99416e+07s, dt:13846.4s, Cycle: 858 +well_1Control: BHP (at the specified reference elevation): 44307029.70932271 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 3.94e-11 ) ; ( R ) = ( 6.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 3.47e-11 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 2.69e-11 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 2.37e-11 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 9.84e-12 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 7.66e-12 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 6.76e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 5.26e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.99e-05 ) ; ( Rwell ) = ( 8.32e-15 ) ; ( R ) = ( 2.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202136 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.99554e+07s, dt:6923.21s, Cycle: 859 +well_1Control: BHP (at the specified reference elevation): 44311224.736229315 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 9.93e-12 ) ; ( R ) = ( 5.67e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44313317.19439073 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0056481 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010101 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.99623e+07s, dt:13846.4s, Cycle: 860 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.52e-09 ) ; ( R ) = ( 1.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 3.97e-11 ) ; ( R ) = ( 6.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 9.99e-12 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 8.84e-12 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 7.82e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.55e-05 ) ; ( Rwell ) = ( 5.20e-15 ) ; ( R ) = ( 3.55e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202362 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.99762e+07s, dt:6923.21s, Cycle: 861 +well_1Control: BHP (at the specified reference elevation): 44317507.80184789 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 6.09e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 6.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00564692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00101244 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.99831e+07s, dt:13846.4s, Cycle: 862 +well_1Control: BHP (at the specified reference elevation): 44319596.814993635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; ( R ) = ( 8.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; ( R ) = ( 7.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 7.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 7.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 6.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 6.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 6.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.02e-05 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 3.02e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0112989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00202681 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.99969e+07s, dt:3057.8s, Cycle: 863 +well_1Control: BHP (at the specified reference elevation): 44323786.83346704 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-04 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 2.69e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.12e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 8.61e-13 ) ; ( R ) = ( 8.00e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00249597 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000447828 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5e+07s, dt:6115.59s, Cycle: 864 +well_1Control: BHP (at the specified reference elevation): 44324708.932442635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 7.35e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 5.53e-15 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00500546 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0008956 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.57532e+07, 2.57937e+07, 2.59028e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.3252e+07, 1.34016e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 738.398 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 20.2626, 718.135 } rm^3 +compflowStatistics, reservoir: Phase mass: { 12665.6, 700461 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1833.03, 216129 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 10832.5, 484332 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 18.6266, 6.18673 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 12646.9, 700455 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 12665.6, 0 }, { 2119.77, 698288 } } kg +well_1Control: BHP (at the specified reference elevation): 44326559.334483676 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.55353e+07, 2.56899e+07, 2.57719e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.3034e+07, 1.32706e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.582 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.582 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219871 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65961.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153910 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219871 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27831e-08, 219871 } } kg +compflowStatistics: Max phase CFL number: 12.3653 +compflowStatistics: Max component CFL number: 16.9936 +Time: 5.00061e+07s, dt:12231.2s, Cycle: 865 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 9.53e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 8.66e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.76e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.96e-06 ) ; ( Rwell ) = ( 1.99e-15 ) ; ( R ) = ( 9.96e-06 ) ; + Last LinSolve(iter,res) = ( 6, 6.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00997438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00179166 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.00183e+07s, dt:6115.59s, Cycle: 866 +well_1Control: BHP (at the specified reference elevation): 44330261.87272844 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 5.39e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 7.64e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 6.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00498613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000895826 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.00245e+07s, dt:12231.2s, Cycle: 867 +well_1Control: BHP (at the specified reference elevation): 44332111.98440309 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 1.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 9.64e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.91e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 5.66e-16 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 7, 3.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00997309 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00179111 +Time: 5.00367e+07s, dt:12231.2s, Cycle: 868 +well_1Control: BHP (at the specified reference elevation): 44335814.238046825 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 7.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.88e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 2.33e-15 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00997012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00178983 +Time: 5.00489e+07s, dt:12231.2s, Cycle: 869 +well_1Control: BHP (at the specified reference elevation): 44339512.418073654 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.17e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 3.14e-15 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00178822 +Time: 5.00612e+07s, dt:12231.2s, Cycle: 870 +well_1Control: BHP (at the specified reference elevation): 44343210.487741545 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 8.84e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.78e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.03e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.89e-06 ) ; ( Rwell ) = ( 7.74e-16 ) ; ( R ) = ( 5.89e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996738 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00178609 +Time: 5.00734e+07s, dt:12231.2s, Cycle: 871 +well_1Control: BHP (at the specified reference elevation): 44346908.21271389 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 9.65e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 8.18e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.37e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.63e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.80e-05 ) ; ( Rwell ) = ( 2.66e-15 ) ; ( R ) = ( 1.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00178335 +Time: 5.00856e+07s, dt:12231.2s, Cycle: 872 +well_1Control: BHP (at the specified reference elevation): 44350605.52604145 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 1.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 9.76e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.89e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.07e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 2.03e-15 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00178 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.00978e+07s, dt:6115.59s, Cycle: 873 +well_1Control: BHP (at the specified reference elevation): 44354302.1890043 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 5.38e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 8.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44356146.20648566 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00498197 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000889615 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.0104e+07s, dt:12231.2s, Cycle: 874 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 9.46e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.02e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 9.47e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.48e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.60e-05 ) ; ( Rwell ) = ( 1.27e-14 ) ; ( R ) = ( 2.60e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996737 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00177886 +Time: 5.01162e+07s, dt:12231.2s, Cycle: 875 +well_1Control: BHP (at the specified reference elevation): 44359840.79410392 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 9.42e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 8.27e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.66e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 1.98e-15 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996148 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00177836 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.01284e+07s, dt:6115.59s, Cycle: 876 +well_1Control: BHP (at the specified reference elevation): 44363536.767388955 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 5.36e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 8.27e-12 ) ; ( R ) = ( 7.66e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00497996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000889273 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.01345e+07s, dt:12231.2s, Cycle: 877 +well_1Control: BHP (at the specified reference elevation): 44365381.02629852 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 9.46e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 9.90e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.69e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.04e-05 ) ; ( Rwell ) = ( 5.15e-15 ) ; ( R ) = ( 2.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00996391 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00177671 +Time: 5.01468e+07s, dt:12231.2s, Cycle: 878 +well_1Control: BHP (at the specified reference elevation): 44369075.16352599 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 9.39e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.15e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.61e-05 ) ; ( Rwell ) = ( 4.62e-16 ) ; ( R ) = ( 2.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00995793 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00177388 +Time: 5.0159e+07s, dt:12231.2s, Cycle: 879 +well_1Control: BHP (at the specified reference elevation): 44372770.332048334 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.10e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.81e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 2.53e-15 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00995611 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00177115 +Time: 5.01712e+07s, dt:12231.2s, Cycle: 880 +well_1Control: BHP (at the specified reference elevation): 44376465.26491765 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.80e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 7.74e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.25e-06 ) ; ( Rwell ) = ( 5.78e-18 ) ; ( R ) = ( 4.25e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00995471 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00176784 +Time: 5.01835e+07s, dt:12231.2s, Cycle: 881 +well_1Control: BHP (at the specified reference elevation): 44380159.67783394 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.40e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 8.31e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.35e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.90e-06 ) ; ( Rwell ) = ( 5.66e-16 ) ; ( R ) = ( 8.90e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00995331 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00176419 +Time: 5.01957e+07s, dt:12231.2s, Cycle: 882 +well_1Control: BHP (at the specified reference elevation): 44383853.81294593 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 9.44e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 8.34e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 8.61e-16 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.39e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44387547.807352915 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00995194 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00176027 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.02079e+07s, dt:6115.59s, Cycle: 883 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 5.33e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 7.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 6.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-04 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 9.49e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00497545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000879856 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.0214e+07s, dt:12231.2s, Cycle: 884 +well_1Control: BHP (at the specified reference elevation): 44389393.310884655 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 9.47e-09 ) ; ( R ) = ( 1.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 8.43e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.48e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.67e-05 ) ; ( Rwell ) = ( 6.24e-15 ) ; ( R ) = ( 2.67e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44393085.60583441 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00995122 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00176441 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.02263e+07s, dt:24462.4s, Cycle: 885 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 2.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 7.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 8.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 5.89e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 5.20e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.57e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.02e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.54e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.12e-05 ) ; ( Rwell ) = ( 4.79e-15 ) ; ( R ) = ( 3.12e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0198961 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0035464 +Time: 5.02507e+07s, dt:24462.4s, Cycle: 886 +well_1Control: BHP (at the specified reference elevation): 44400469.31150217 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 9.47e-09 ) ; ( R ) = ( 2.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.18e-10 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.74e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.82e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-05 ) ; ( Rwell ) = ( 3.55e-15 ) ; ( R ) = ( 2.38e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44407853.99789427 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0198906 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00355884 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.02752e+07s, dt:48924.7s, Cycle: 887 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 4.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 4.74e-10 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 8.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.67e-10 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 3.23e-10 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 7.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.84e-10 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.41e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.49e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.27e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.19e-10 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.39e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.93e-10 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.49e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.23e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.92e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.31e-10 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.40e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.16e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.90e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.61e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.48e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 8.93e-11 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.50e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.60e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 7.85e-11 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.43e-03 ) ; ( Rwell ) = ( 6.92e-11 ) ; ( R ) = ( 9.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 8.91e-03 ) ; ( Rwell ) = ( 6.09e-11 ) ; ( R ) = ( 8.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.75e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 8.29e-03 ) ; ( Rwell ) = ( 5.35e-11 ) ; ( R ) = ( 8.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 1.94e-14 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.71e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44422595.00226115 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0397672 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00714091 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.03241e+07s, dt:24462.4s, Cycle: 888 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 7.04e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.22e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 9.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 9.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0198712 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00357691 +Time: 5.03486e+07s, dt:24462.4s, Cycle: 889 +well_1Control: BHP (at the specified reference elevation): 44429968.02550374 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 6.83e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 5.97e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 5.25e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 4.62e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 4.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.58e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.84e-05 ) ; ( Rwell ) = ( 2.59e-14 ) ; ( R ) = ( 4.84e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0198687 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00357899 +Time: 5.03731e+07s, dt:24462.4s, Cycle: 890 +well_1Control: BHP (at the specified reference elevation): 44437344.01125941 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 5.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 6.79e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 5.98e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.28e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.63e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.08e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.16e-05 ) ; ( Rwell ) = ( 1.09e-14 ) ; ( R ) = ( 3.16e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0198621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00357691 +Time: 5.03975e+07s, dt:24462.4s, Cycle: 891 +well_1Control: BHP (at the specified reference elevation): 44444718.99223226 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 6.79e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 5.96e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.24e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.57e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.02e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.63e-11 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.95e-05 ) ; ( Rwell ) = ( 3.44e-15 ) ; ( R ) = ( 3.95e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0198563 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00357103 +Time: 5.0422e+07s, dt:24462.4s, Cycle: 892 +well_1Control: BHP (at the specified reference elevation): 44452094.57002403 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.70e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 3.06e-15 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0198506 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00356122 +Time: 5.04464e+07s, dt:24462.4s, Cycle: 893 +well_1Control: BHP (at the specified reference elevation): 44459470.314027846 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 6.81e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.23e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.60e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.05e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.57e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.09e-05 ) ; ( Rwell ) = ( 1.15e-14 ) ; ( R ) = ( 3.09e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44466845.171750605 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0198448 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00358528 +Time: 5.04709e+07s, dt:24462.4s, Cycle: 894 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 2.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 6.70e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.11e-11 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.49e-11 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 6.62e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44474211.10093875 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0198341 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00360841 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.04954e+07s, dt:48924.7s, Cycle: 895 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 9.40e-09 ) ; ( R ) = ( 4.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 4.71e-10 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 8.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 8.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 4.14e-10 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 8.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 3.63e-10 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-03 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.19e-10 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.81e-10 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.65e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.87e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 2.48e-10 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.51e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.75e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.17e-10 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.47e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 1.22e-10 ) ; ( R ) = ( 9.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.50e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.09e-10 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.67e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 9.59e-11 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.43e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.20e-03 ) ; ( Rwell ) = ( 8.32e-11 ) ; ( R ) = ( 7.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.56e-05 ) ; ( Rwell ) = ( 5.19e-14 ) ; ( R ) = ( 7.56e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0396626 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00726882 +Time: 5.05443e+07s, dt:48924.7s, Cycle: 896 +well_1Control: BHP (at the specified reference elevation): 44488936.82749124 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 9.40e-09 ) ; ( R ) = ( 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.69e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 2.68e-10 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.36e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 2.07e-10 ) ; ( R ) = ( 6.88e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.57e-03 ) ; ( Rwell ) = ( 5.24e-11 ) ; ( R ) = ( 8.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 4.61e-11 ) ; ( R ) = ( 8.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 4.05e-11 ) ; ( R ) = ( 7.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 3.57e-11 ) ; ( R ) = ( 7.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 7.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 6.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 6.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 9.59e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 8.99e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 8.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 7.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 7.35e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0396393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00734506 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.05932e+07s, dt:24462.4s, Cycle: 897 +well_1Control: BHP (at the specified reference elevation): 44503650.88599459 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; ( R ) = ( 2.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.19e-10 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.03e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 7.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44511013.28619235 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0198063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00368292 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.06177e+07s, dt:48924.7s, Cycle: 898 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; ( R ) = ( 4.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 4.74e-10 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 7.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 8.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.64e-10 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 7.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 3.20e-10 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 7.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.82e-10 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.48e-10 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.59e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 2.18e-10 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.92e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.91e-10 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.68e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.69e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.22e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.48e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.30e-10 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.89e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.01e-10 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.96e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 8.86e-11 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 7.79e-11 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 6.85e-11 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 6.03e-11 ) ; ( R ) = ( 9.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 8.39e-05 ) ; ( Rwell ) = ( 5.30e-14 ) ; ( R ) = ( 8.39e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0396051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00737146 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.06666e+07s, dt:24462.4s, Cycle: 899 +well_1Control: BHP (at the specified reference elevation): 44525735.83813495 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; ( R ) = ( 2.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 1.19e-10 ) ; ( R ) = ( 5.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 6.80e-11 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 5.99e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 5.26e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.63e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.08e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.80e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.24e-05 ) ; ( Rwell ) = ( 7.03e-15 ) ; ( R ) = ( 5.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.91e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44533100.49419367 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0197928 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00368092 +Time: 5.06911e+07s, dt:24462.4s, Cycle: 900 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; ( R ) = ( 2.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 6.58e-11 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.92e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.61e-06 ) ; ( Rwell ) = ( 3.39e-14 ) ; ( R ) = ( 8.61e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0197874 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00367097 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.07155e+07s, dt:48924.7s, Cycle: 901 +well_1Control: BHP (at the specified reference elevation): 44540465.058751926 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 9.38e-09 ) ; ( R ) = ( 4.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 3.59e-10 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 3.16e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.02e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 2.78e-10 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 2.44e-10 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.15e-10 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.20e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.89e-10 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.20e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.20e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.70e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.66e-10 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.69e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.67e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.46e-10 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.89e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.59e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.29e-10 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.13e-10 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.44e-05 ) ; ( Rwell ) = ( 6.91e-14 ) ; ( R ) = ( 8.44e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0395607 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00728704 +Time: 5.07644e+07s, dt:48924.7s, Cycle: 902 +well_1Control: BHP (at the specified reference elevation): 44555178.29731569 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; ( R ) = ( 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.64e-10 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.66e-10 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.05e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.22e-10 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.07e-10 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 9.43e-11 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 8.31e-11 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 7.30e-11 ) ; ( R ) = ( 9.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 6.42e-11 ) ; ( R ) = ( 9.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.66e-03 ) ; ( Rwell ) = ( 5.65e-11 ) ; ( R ) = ( 8.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 4.97e-11 ) ; ( R ) = ( 7.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 4.37e-11 ) ; ( R ) = ( 6.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.29e-03 ) ; ( Rwell ) = ( 3.86e-11 ) ; ( R ) = ( 7.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 6.93e-03 ) ; ( Rwell ) = ( 3.40e-11 ) ; ( R ) = ( 6.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 2.64e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 24462.374114990234 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 9.36e-09 ) ; ( R ) = ( 2.21e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 1.19e-10 ) ; ( R ) = ( 5.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 6.76e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 4.56e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44562526.82941879 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0197685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00365939 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 24462.374114990234, remaining dt = 24462.374114990234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; ( R ) = ( 2.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 1.18e-10 ) ; ( R ) = ( 5.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 6.61e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 5.81e-11 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 5.10e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.54e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 8.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.77e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 9.88e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44569876.70611941 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0197671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00366798 +Time: 5.08134e+07s, dt:24462.4s, Cycle: 903 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 9.33e-09 ) ; ( R ) = ( 2.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.19e-10 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.00e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.64e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.67e-05 ) ; ( Rwell ) = ( 2.98e-14 ) ; ( R ) = ( 7.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44577228.0514608 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0197601 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00367411 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.08378e+07s, dt:48924.7s, Cycle: 904 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 9.33e-09 ) ; ( R ) = ( 4.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 4.72e-10 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 8.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.61e-10 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.53e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 7.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 3.18e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 7.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 2.79e-10 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 7.04e-11 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.54e-05 ) ; ( Rwell ) = ( 2.59e-14 ) ; ( R ) = ( 4.54e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0395059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00734398 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.08868e+07s, dt:97849.5s, Cycle: 905 +well_1Control: BHP (at the specified reference elevation): 44591916.63216572 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; ( R ) = ( 8.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.22e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 9.41e-09 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.20e-04 ) ; ( Rwell ) = ( 1.86e-12 ) ; ( R ) = ( 2.20e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0789528 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0144354 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.09846e+07s, dt:15389.4s, Cycle: 906 +well_1Control: BHP (at the specified reference elevation): 44621242.75440649 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 9.30e-09 ) ; ( R ) = ( 1.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.58e-11 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 6.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 8.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 4.02e-11 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.06e-05 ) ; ( Rwell ) = ( 1.07e-14 ) ; ( R ) = ( 5.06e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0124069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00226839 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.1e+07s, dt:30778.9s, Cycle: 907 +well_1Control: BHP (at the specified reference elevation): 44625868.68730501 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 9.32e-09 ) ; ( R ) = ( 2.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.85e-10 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 4.74e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 4.17e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 1.07e-14 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.36e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44635107.99358957 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0248083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00453452 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.59654e+07, 2.60059e+07, 2.61151e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.34591e+07, 1.36088e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 738.552 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 20.5809, 717.971 } rm^3 +compflowStatistics, reservoir: Phase mass: { 12933.2, 700417 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1869.39, 216211 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 11063.8, 484206 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 18.676, 6.46258 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 12914.6, 700410 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 12933.2, 0 }, { 2155.08, 698208 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.57482e+07, 2.59023e+07, 2.59841e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.32418e+07, 1.34777e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.63 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.63 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 219951 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 65985.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 153966 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 219951 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.27914e-08, 219951 } } kg +compflowStatistics: Max phase CFL number: 61.8918 +compflowStatistics: Max component CFL number: 85.0586 +Time: 5.10308e+07s, dt:15389.4s, Cycle: 908 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.29e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.77e-11 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.67e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 9.47e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.59e-05 ) ; ( Rwell ) = ( 7.77e-15 ) ; ( R ) = ( 2.59e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0124007 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00226476 +Time: 5.10462e+07s, dt:15389.4s, Cycle: 909 +well_1Control: BHP (at the specified reference elevation): 44639728.963520974 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.29e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.62e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-05 ) ; ( Rwell ) = ( 5.35e-15 ) ; ( R ) = ( 4.90e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123985 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00226367 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.10616e+07s, dt:30778.9s, Cycle: 910 +well_1Control: BHP (at the specified reference elevation): 44644349.281386495 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 9.29e-09 ) ; ( R ) = ( 2.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 8.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.31e-03 ) ; ( Rwell ) = ( 1.05e-10 ) ; ( R ) = ( 6.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 9.23e-11 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 8.12e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 7.11e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 6.17e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 5.52e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 4.89e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 4.30e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.18e-05 ) ; ( Rwell ) = ( 1.69e-14 ) ; ( R ) = ( 3.18e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00452157 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.10923e+07s, dt:15389.4s, Cycle: 911 +well_1Control: BHP (at the specified reference elevation): 44653584.07829326 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.28e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.67e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 8.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.012387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00225712 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.11077e+07s, dt:30778.9s, Cycle: 912 +well_1Control: BHP (at the specified reference elevation): 44658196.09092562 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 9.25e-09 ) ; ( R ) = ( 2.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.49e-03 ) ; ( Rwell ) = ( 1.87e-10 ) ; ( R ) = ( 8.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 6.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 9.34e-11 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 8.08e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.87e-03 ) ; ( Rwell ) = ( 7.10e-11 ) ; ( R ) = ( 5.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 6.24e-11 ) ; ( R ) = ( 5.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 5.49e-11 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 4.82e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 1.73e-14 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.23e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44667430.59086077 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0247782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00449419 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.11385e+07s, dt:15389.4s, Cycle: 913 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.28e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.65e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.96e-05 ) ; ( Rwell ) = ( 8.77e-15 ) ; ( R ) = ( 3.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123847 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00224065 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.11539e+07s, dt:30778.9s, Cycle: 914 +well_1Control: BHP (at the specified reference elevation): 44672049.608667254 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 9.28e-09 ) ; ( R ) = ( 2.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.79e-03 ) ; ( Rwell ) = ( 1.86e-10 ) ; ( R ) = ( 9.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.05e-10 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.98e-11 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 5.27e-11 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 4.63e-11 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 9.47e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 9.56e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.20e-05 ) ; ( Rwell ) = ( 7.76e-15 ) ; ( R ) = ( 3.20e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00445676 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.11847e+07s, dt:15389.4s, Cycle: 915 +well_1Control: BHP (at the specified reference elevation): 44681280.99436951 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.29e-10 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.14e-10 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.13e-10 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.12e-10 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.12e-10 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.11e-10 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.08e-10 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.07e-10 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.07e-10 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.07e-10 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.84e-06 ) ; ( Rwell ) = ( 4.80e-14 ) ; ( R ) = ( 6.84e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00222513 +Time: 5.12001e+07s, dt:15389.4s, Cycle: 916 +well_1Control: BHP (at the specified reference elevation): 44685898.67808916 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; ( R ) = ( 1.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.64e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 4.94e-15 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123765 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00222256 +Time: 5.12155e+07s, dt:15389.4s, Cycle: 917 +well_1Control: BHP (at the specified reference elevation): 44690516.34206157 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; ( R ) = ( 1.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 4.69e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 9.61e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.10e-05 ) ; ( Rwell ) = ( 8.04e-15 ) ; ( R ) = ( 1.10e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123745 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00222752 +Time: 5.12308e+07s, dt:15389.4s, Cycle: 918 +well_1Control: BHP (at the specified reference elevation): 44695133.43446757 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; ( R ) = ( 1.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.68e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.66e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.35e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 2.76e-15 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123725 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0022357 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.12462e+07s, dt:30778.9s, Cycle: 919 +well_1Control: BHP (at the specified reference elevation): 44699750.19238956 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 9.27e-09 ) ; ( R ) = ( 2.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 1.86e-10 ) ; ( R ) = ( 9.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 1.05e-10 ) ; ( R ) = ( 7.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 6.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 9.23e-11 ) ; ( R ) = ( 7.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 8.12e-11 ) ; ( R ) = ( 6.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.44e-03 ) ; ( Rwell ) = ( 7.15e-11 ) ; ( R ) = ( 6.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 6.21e-11 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 5.46e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.80e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.22e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.44e-05 ) ; ( Rwell ) = ( 3.06e-14 ) ; ( R ) = ( 2.44e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0044958 +Time: 5.1277e+07s, dt:30778.9s, Cycle: 920 +well_1Control: BHP (at the specified reference elevation): 44708966.63000129 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 9.23e-09 ) ; ( R ) = ( 2.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 7.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.91e-03 ) ; ( Rwell ) = ( 1.04e-10 ) ; ( R ) = ( 6.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 9.13e-11 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.98e-03 ) ; ( Rwell ) = ( 8.03e-11 ) ; ( R ) = ( 5.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 7.05e-11 ) ; ( R ) = ( 5.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 6.20e-11 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 5.48e-11 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 4.82e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.85e-05 ) ; ( Rwell ) = ( 3.01e-15 ) ; ( R ) = ( 3.85e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247331 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00450993 +Time: 5.13078e+07s, dt:30778.9s, Cycle: 921 +well_1Control: BHP (at the specified reference elevation): 44718183.02161155 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 9.23e-09 ) ; ( R ) = ( 2.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.37e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 8.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 1.04e-10 ) ; ( R ) = ( 6.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 9.12e-11 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 8.03e-11 ) ; ( R ) = ( 6.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 7.12e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 6.27e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 5.52e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 4.86e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 4.23e-11 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.63e-05 ) ; ( Rwell ) = ( 1.67e-14 ) ; ( R ) = ( 1.63e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247248 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00451327 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.13386e+07s, dt:15389.4s, Cycle: 922 +well_1Control: BHP (at the specified reference elevation): 44727397.190975636 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 9.22e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.62e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 8.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123537 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0022564 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.1354e+07s, dt:30778.9s, Cycle: 923 +well_1Control: BHP (at the specified reference elevation): 44732000.73039764 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; ( R ) = ( 2.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 1.83e-10 ) ; ( R ) = ( 8.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 6.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 9.07e-11 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 8.00e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 7.02e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 6.19e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 5.42e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 4.80e-11 ) ; ( R ) = ( 5.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 4.22e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.28e-05 ) ; ( Rwell ) = ( 1.99e-15 ) ; ( R ) = ( 7.28e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44741210.97390002 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0247134 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00450174 +Time: 5.13847e+07s, dt:30778.9s, Cycle: 924 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 9.22e-09 ) ; ( R ) = ( 2.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.38e-03 ) ; ( Rwell ) = ( 1.83e-10 ) ; ( R ) = ( 8.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.04e-10 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 9.13e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 8.04e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.07e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.96e-05 ) ; ( Rwell ) = ( 4.61e-16 ) ; ( R ) = ( 3.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.69e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44750418.76595318 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0247041 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00448164 +Time: 5.14155e+07s, dt:30778.9s, Cycle: 925 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 2.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.76e-05 ) ; ( Rwell ) = ( 1.19e-12 ) ; ( R ) = ( 3.76e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.67e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44759625.348464444 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0246962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00445345 +Time: 5.14463e+07s, dt:30778.9s, Cycle: 926 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 2.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.82e-10 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 4.60e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.59e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.54e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 8.49e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 6.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 9.56e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 5.97e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 8.97e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 5.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 8.41e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 9.81e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 5.25e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 7.88e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 9.20e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 9.85e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 4.92e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 7.39e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 8.62e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 9.24e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 4.61e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 6.93e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.10e-12 ) ; ( R ) = ( 8.37e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0246887 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00441703 +Time: 5.14771e+07s, dt:30778.9s, Cycle: 927 +well_1Control: BHP (at the specified reference elevation): 44768829.69585469 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 9.20e-09 ) ; ( R ) = ( 2.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 1.82e-10 ) ; ( R ) = ( 9.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 9.02e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 7.98e-11 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 7.02e-11 ) ; ( R ) = ( 5.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 6.17e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 5.43e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 4.79e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 4.22e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.71e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.12e-05 ) ; ( Rwell ) = ( 8.66e-16 ) ; ( R ) = ( 4.12e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0246801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00441708 +Time: 5.15079e+07s, dt:30778.9s, Cycle: 928 +well_1Control: BHP (at the specified reference elevation): 44778023.25808774 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 9.18e-09 ) ; ( R ) = ( 2.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 1.83e-10 ) ; ( R ) = ( 9.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 6.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 9.04e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-04 ) ; ( Rwell ) = ( 7.95e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.51e-12 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.02467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00442907 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.15386e+07s, dt:61557.8s, Cycle: 929 +well_1Control: BHP (at the specified reference elevation): 44787211.58807907 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 9.16e-09 ) ; ( R ) = ( 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 7.25e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 8.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.57e-10 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 7.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 4.90e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 6.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.31e-10 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.24e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 3.79e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.34e-10 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.92e-03 ) ; ( Rwell ) = ( 2.93e-10 ) ; ( R ) = ( 8.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.41e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.13e-03 ) ; ( Rwell ) = ( 2.57e-10 ) ; ( R ) = ( 9.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.27e-10 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.85e-05 ) ; ( Rwell ) = ( 3.33e-14 ) ; ( R ) = ( 6.85e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0493225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00885875 +Time: 5.16002e+07s, dt:61557.8s, Cycle: 930 +well_1Control: BHP (at the specified reference elevation): 44805570.096923634 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 9.15e-09 ) ; ( R ) = ( 5.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 7.24e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 4.09e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.76e-03 ) ; ( Rwell ) = ( 3.60e-10 ) ; ( R ) = ( 9.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 3.17e-10 ) ; ( R ) = ( 9.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 2.78e-10 ) ; ( R ) = ( 8.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.06e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 2.45e-10 ) ; ( R ) = ( 8.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.62e-03 ) ; ( Rwell ) = ( 2.15e-10 ) ; ( R ) = ( 7.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.09e-03 ) ; ( Rwell ) = ( 1.89e-10 ) ; ( R ) = ( 7.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.67e-10 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.89e-05 ) ; ( Rwell ) = ( 7.31e-14 ) ; ( R ) = ( 9.89e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0492872 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0087929 +Time: 5.16617e+07s, dt:61557.8s, Cycle: 931 +well_1Control: BHP (at the specified reference elevation): 44823930.518155426 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 9.15e-09 ) ; ( R ) = ( 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.32e-08 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.87e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44842286.92105946 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0492516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00871634 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.17233e+07s, dt:123116s, Cycle: 932 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 9.15e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 6.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.28e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 6.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 7.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 6.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.95e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 9.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.18e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; ( R ) = ( 9.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 6.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 3.12e-13 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.29e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44878865.651328295 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0984017 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0174734 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.18464e+07s, dt:153581s, Cycle: 933 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 9.08e-09 ) ; ( R ) = ( 1.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 7.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 6.49e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.60e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 8.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 8.51e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.84e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 9.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 9.57e-10 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 8.42e-10 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 7.40e-10 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 6.51e-10 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.83e-03 ) ; ( Rwell ) = ( 5.71e-10 ) ; ( R ) = ( 7.83e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.68e-04 ) ; ( Rwell ) = ( 9.19e-14 ) ; ( R ) = ( 1.68e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.18e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44924456.54242754 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.12253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0219752 +Time: 5.2e+07s, dt:153581s, Cycle: 934 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 9.06e-09 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.99e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 6.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.34e-10 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.06e-05 ) ; ( Rwell ) = ( 2.93e-13 ) ; ( R ) = ( 7.06e-05 ) ; + Last LinSolve(iter,res) = ( 11, 5.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 44970012.50976222 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.122281 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0220999 +compflowStatistics, reservoir: Pressure (min, average, max): 2.6197e+07, 2.62374e+07, 2.63468e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.36654e+07, 1.38152e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 738.72 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 20.9274, 717.793 } rm^3 +compflowStatistics, reservoir: Phase mass: { 13225.9, 700370 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1909.1, 216301 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 11316.8, 484069 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.1347, 6.60162 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 13206.7, 700363 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 13225.9, 0 }, { 2194.41, 698121 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.59807e+07, 2.61341e+07, 2.62156e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.3449e+07, 1.3684e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.681 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.681 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220039 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66011.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154027 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220039 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28005e-08, 220039 } } kg +compflowStatistics: Max phase CFL number: 307.023 +compflowStatistics: Max component CFL number: 421.942 +Time: 5.21536e+07s, dt:153581s, Cycle: 935 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 9.03e-09 ) ; ( R ) = ( 1.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 8.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 9.88e-10 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 7.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 8.70e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 7.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 7.65e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 6.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 9.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 6.72e-10 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 9.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 5.91e-10 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 9.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 5.20e-10 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 6.61e-14 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.122043 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0222513 +Time: 5.23072e+07s, dt:153581s, Cycle: 936 +well_1Control: BHP (at the specified reference elevation): 45015562.25929298 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 9.01e-09 ) ; ( R ) = ( 1.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 1.63e-10 ) ; ( R ) = ( 6.58e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.30e-05 ) ; ( Rwell ) = ( 1.36e-13 ) ; ( R ) = ( 8.30e-05 ) ; + Last LinSolve(iter,res) = ( 10, 6.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.121824 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0221112 +Time: 5.24607e+07s, dt:153581s, Cycle: 937 +well_1Control: BHP (at the specified reference elevation): 45061131.249188066 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 8.99e-09 ) ; ( R ) = ( 1.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.38e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 6.11e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 5.37e-10 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.03e-10 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 9.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 2.67e-10 ) ; ( R ) = ( 8.76e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.90e-05 ) ; ( Rwell ) = ( 2.26e-14 ) ; ( R ) = ( 8.90e-05 ) ; + Last LinSolve(iter,res) = ( 10, 6.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 45106622.57564983 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.12162 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0217369 +Time: 5.26143e+07s, dt:153581s, Cycle: 938 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 8.95e-09 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 7.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 4.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 4.52e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.31e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 9.97e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 6.40e-10 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 7.08e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 8.62e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 9.32e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.62e-10 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 3.25e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 6.64e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.17e-10 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.70e-04 ) ; ( Rwell ) = ( 1.42e-13 ) ; ( R ) = ( 1.70e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.121423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0215013 +Time: 5.27679e+07s, dt:153581s, Cycle: 939 +well_1Control: BHP (at the specified reference elevation): 45152076.42390691 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 8.92e-09 ) ; ( R ) = ( 1.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 9.29e-09 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 9.06e-09 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 8.87e-09 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 8.67e-09 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 8.50e-09 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 8.35e-09 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.22e-09 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 8.11e-09 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 7.99e-09 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.01e-04 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 3.01e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.12123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0213002 +Time: 5.29215e+07s, dt:78515.8s, Cycle: 940 +well_1Control: BHP (at the specified reference elevation): 45197476.82168734 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 8.89e-09 ) ; ( R ) = ( 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 2.89e-10 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 2.54e-10 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.96e-10 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.95e-05 ) ; ( Rwell ) = ( 1.75e-14 ) ; ( R ) = ( 5.95e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0618923 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0107828 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.3e+07s, dt:157032s, Cycle: 941 +well_1Control: BHP (at the specified reference elevation): 45220716.73308785 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 8.88e-09 ) ; ( R ) = ( 1.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 9.18e-09 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 6.00e-09 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.51e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 9.51e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.00e-04 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 2.00e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.123666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0215165 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 2.64034e+07, 2.64438e+07, 2.65533e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.38711e+07, 1.40211e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 738.87 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 21.2361, 717.634 } rm^3 +compflowStatistics, reservoir: Phase mass: { 13487.6, 700328 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1944.99, 216380 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 11542.7, 483947 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.3996, 6.74048 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 13468.2, 700321 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 13487.6, 0 }, { 2229.33, 698043 } } kg +well_1Control: BHP (at the specified reference elevation): 45267038.71709447 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.61876e+07, 2.63406e+07, 2.6422e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.36553e+07, 1.38897e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.727 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.727 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220117 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66035.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154082 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220117 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28085e-08, 220117 } } kg +compflowStatistics: Max phase CFL number: 312.32 +compflowStatistics: Max component CFL number: 429.216 +Time: 5.3157e+07s, dt:291743s, Cycle: 942 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 8.84e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 6.31e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 12, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 6.73e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 12, 7.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.229199 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0393822 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.34488e+07s, dt:411833s, Cycle: 943 +well_1Control: BHP (at the specified reference elevation): 45352670.618875876 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 8.77e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 9.75e-08 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 18, 8.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 1.19e-12 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 13, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.71e-03 ) ; ( Rwell ) = ( 1.37e-12 ) ; ( R ) = ( 7.71e-03 ) ; + Last LinSolve(iter,res) = ( 13, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.15e-04 ) ; ( Rwell ) = ( 3.75e-16 ) ; ( R ) = ( 1.15e-04 ) ; + Last LinSolve(iter,res) = ( 15, 9.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.322074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561743 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.38606e+07s, dt:139392s, Cycle: 944 +well_1Control: BHP (at the specified reference elevation): 45473016.40075675 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 8.67e-09 ) ; ( R ) = ( 1.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 1.06e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 4.27e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 6.25e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 9.21e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 3.89e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 5.36e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 7.96e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.40e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.52e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.59e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 6.87e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 2.99e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.19e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 3.92e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 5.92e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 2.64e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.90e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 3.34e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 5.09e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 2.35e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.69e-11 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 5.87e-10 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 5.69e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.27e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.75e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.16e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.09e-05 ) ; ( Rwell ) = ( 2.33e-13 ) ; ( R ) = ( 8.09e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.108617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0186408 +Time: 5.4e+07s, dt:139392s, Cycle: 945 +well_1Control: BHP (at the specified reference elevation): 45514044.92096633 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 8.70e-09 ) ; ( R ) = ( 1.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 9.65e-09 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 8.95e-09 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 6.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 8.34e-09 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 8.08e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 7.92e-09 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 7.60e-09 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 7.46e-09 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 7.31e-09 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 6.96e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 6.87e-09 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 6.79e-09 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 6.73e-09 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 9.78e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 6.69e-09 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 5.19e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 6.66e-09 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 8.66e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 6.65e-09 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 9.85e-05 ) ; ( Rwell ) = ( 1.20e-12 ) ; ( R ) = ( 9.85e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.108488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0184638 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.66044e+07, 2.66448e+07, 2.67545e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.40757e+07, 1.42258e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.017 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 21.5355, 717.481 } rm^3 +compflowStatistics, reservoir: Phase mass: { 13742.6, 700288 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 1980.17, 216458 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 11762.5, 483830 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.4143, 7.09907 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 13723.2, 700281 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 13742.6, 0 }, { 2264.8, 697967 } } kg +well_1Control: BHP (at the specified reference elevation): 45555004.5409939 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.63894e+07, 2.65418e+07, 2.6623e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.38608e+07, 1.40944e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.772 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220193 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66057.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154135 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220193 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28164e-08, 220193 } } kg +compflowStatistics: Max phase CFL number: 275.885 +compflowStatistics: Max component CFL number: 379.138 +Time: 5.41394e+07s, dt:69696s, Cycle: 946 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 8.67e-09 ) ; ( R ) = ( 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.65e-03 ) ; ( Rwell ) = ( 8.64e-10 ) ; ( R ) = ( 9.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.21e-10 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.12e-05 ) ; ( Rwell ) = ( 1.13e-13 ) ; ( R ) = ( 6.12e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0541874 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00915657 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.42091e+07s, dt:139392s, Cycle: 947 +well_1Control: BHP (at the specified reference elevation): 45575503.29340953 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 8.66e-09 ) ; ( R ) = ( 1.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-03 ) ; ( Rwell ) = ( 7.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 6.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 7.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 6.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 6.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 9.48e-10 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 8.33e-10 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.75e-03 ) ; ( Rwell ) = ( 2.11e-10 ) ; ( R ) = ( 9.75e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.39e-05 ) ; ( Rwell ) = ( 2.36e-13 ) ; ( R ) = ( 4.39e-05 ) ; + Last LinSolve(iter,res) = ( 10, 6.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.10833 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0184223 +Time: 5.43485e+07s, dt:139392s, Cycle: 948 +well_1Control: BHP (at the specified reference elevation): 45616373.39125364 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 8.62e-09 ) ; ( R ) = ( 1.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 3.11e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 6.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 3.54e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 3.02e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 5.21e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.19e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.88e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.89e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 4.70e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.98e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 2.73e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.76e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 4.26e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.79e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.60e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.64e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 3.85e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.61e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 2.46e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.51e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 8.89e-10 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 3.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 2.44e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.34e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.39e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 7.82e-10 ) ; ( R ) = ( 3.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.15e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.28e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.27e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 6.88e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.85e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.73e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.75e-05 ) ; ( Rwell ) = ( 1.17e-13 ) ; ( R ) = ( 6.75e-05 ) ; + Last LinSolve(iter,res) = ( 9, 9.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 45657180.93409678 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.108222 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0184726 +Time: 5.44879e+07s, dt:139392s, Cycle: 949 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 8.59e-09 ) ; ( R ) = ( 1.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 9.81e-09 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 6.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.93e-03 ) ; ( Rwell ) = ( 7.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 9.06e-09 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 7.97e-09 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 7.81e-09 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 7.67e-09 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 7.56e-09 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 7.41e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 7.07e-09 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 7.01e-09 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 6.83e-09 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.20e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 6.80e-09 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.19e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.91e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; ( R ) = ( 8.91e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.47e-05 ) ; ( Rwell ) = ( 3.70e-13 ) ; ( R ) = ( 7.47e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.108101 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.018302 +Time: 5.46273e+07s, dt:139392s, Cycle: 950 +well_1Control: BHP (at the specified reference elevation): 45697921.98200843 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 8.56e-09 ) ; ( R ) = ( 1.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 7.44e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.68e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 9.27e-10 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 8.15e-10 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 7.16e-10 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 2.69e-13 ) ; ( R ) = ( 2.10e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.21e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 45738606.439792246 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.10797 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0182125 +Time: 5.47667e+07s, dt:139392s, Cycle: 951 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 8.53e-09 ) ; ( R ) = ( 1.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.31e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 8.97e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.25e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 6.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 8.23e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 5.64e-10 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.42e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 6.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 1.25e-10 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 6.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.10e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.31e-05 ) ; ( Rwell ) = ( 1.79e-15 ) ; ( R ) = ( 2.31e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.10783 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0181218 +Time: 5.4906e+07s, dt:93952.6s, Cycle: 952 +well_1Control: BHP (at the specified reference elevation): 45779260.25028516 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.53e-03 ) ; ( Rwell ) = ( 8.51e-09 ) ; ( R ) = ( 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 8.66e-10 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-04 ) ; ( Rwell ) = ( 9.68e-14 ) ; ( R ) = ( 2.45e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0725916 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0122348 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.5e+07s, dt:187905s, Cycle: 953 +well_1Control: BHP (at the specified reference elevation): 45806652.28948402 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 8.48e-09 ) ; ( R ) = ( 1.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; ( R ) = ( 7.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; ( R ) = ( 6.97e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 3.11e-08 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 8.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 9.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 5.43e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 2.16e-13 ) ; ( R ) = ( 4.11e-04 ) ; + Last LinSolve(iter,res) = ( 10, 7.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.14501 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0246436 +well_1Control: BHP (at the specified reference elevation): 45861266.74882212 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.68192e+07, 2.68596e+07, 2.69694e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.42808e+07, 1.4431e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.173 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 21.8573, 717.315 } rm^3 +compflowStatistics, reservoir: Phase mass: { 14017.2, 700244 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2016.65, 216541 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 12000.5, 483703 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.0246, 7.73392 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 13997.1, 700236 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 14017.2, 0 }, { 2300.28, 697886 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.66045e+07, 2.67568e+07, 2.68378e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.40659e+07, 1.42995e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.819 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.819 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220274 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66082.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154192 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220274 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28249e-08, 220274 } } kg +compflowStatistics: Max phase CFL number: 370.003 +compflowStatistics: Max component CFL number: 508.472 +Time: 5.51879e+07s, dt:187905s, Cycle: 954 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 8.44e-09 ) ; ( R ) = ( 1.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 9.66e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 4.47e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.13e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 3.55e-04 ) ; + Last LinSolve(iter,res) = ( 10, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.144724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0252418 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.53758e+07s, dt:93952.6s, Cycle: 955 +well_1Control: BHP (at the specified reference elevation): 45915846.366819814 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.76e-03 ) ; ( Rwell ) = ( 8.41e-09 ) ; ( R ) = ( 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.79e-03 ) ; ( Rwell ) = ( 3.87e-10 ) ; ( R ) = ( 7.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 9.69e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 8.84e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.36e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 9.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0722393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0126514 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.54698e+07s, dt:187905s, Cycle: 956 +well_1Control: BHP (at the specified reference elevation): 45943179.54840188 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 8.40e-09 ) ; ( R ) = ( 1.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; ( R ) = ( 7.56e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 7.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 2.56e-08 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 6.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 3.74e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 9.83e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; ( R ) = ( 4.06e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 7.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.21e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.88e-04 ) ; ( Rwell ) = ( 2.92e-13 ) ; ( R ) = ( 2.88e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.144318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0250938 +Time: 5.56577e+07s, dt:187905s, Cycle: 957 +well_1Control: BHP (at the specified reference elevation): 45997667.862240866 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 8.36e-09 ) ; ( R ) = ( 1.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 8.49e-09 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 8.07e-09 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 7.76e-09 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.08e-02 ) ; ( Rwell ) = ( 7.44e-09 ) ; ( R ) = ( 8.08e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.85e-02 ) ; ( Rwell ) = ( 7.18e-09 ) ; ( R ) = ( 7.85e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 6.97e-09 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.50e-04 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 10, 7.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.144043 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0246654 +Time: 5.58456e+07s, dt:154427s, Cycle: 958 +well_1Control: BHP (at the specified reference elevation): 46052078.01652305 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 8.32e-09 ) ; ( R ) = ( 1.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 3.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 4.76e-14 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.118166 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0198202 +Time: 5.6e+07s, dt:154427s, Cycle: 959 +well_1Control: BHP (at the specified reference elevation): 46096776.79413611 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 8.30e-09 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 6.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 7.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 5.30e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 8.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 9.39e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.99e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.07e-05 ) ; ( Rwell ) = ( 2.81e-14 ) ; ( R ) = ( 8.07e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0200639 +compflowStatistics, reservoir: Pressure (min, average, max): 2.70166e+07, 2.7057e+07, 2.71669e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.44851e+07, 1.46354e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.316 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 22.1525, 717.164 } rm^3 +compflowStatistics, reservoir: Phase mass: { 14270, 700203 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2050.79, 216617 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 12219.2, 483586 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.5924, 7.94199 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 14250.4, 700195 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 14270, 0 }, { 2333.26, 697811 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.68023e+07, 2.69543e+07, 2.70352e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.42708e+07, 1.45037e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.863 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.863 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220348 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66104.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154244 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220348 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28332e-08, 220348 } } kg +well_1Control: BHP (at the specified reference elevation): 46141418.00226871 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 302.68 +compflowStatistics: Max component CFL number: 415.945 +Time: 5.61544e+07s, dt:154427s, Cycle: 960 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 8.27e-09 ) ; ( R ) = ( 1.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 4.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 9.16e-10 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 8.06e-10 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 7.09e-10 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 4.23e-13 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 10, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117798 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0200801 +Time: 5.63089e+07s, dt:154427s, Cycle: 961 +well_1Control: BHP (at the specified reference elevation): 46185977.66666638 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 8.24e-09 ) ; ( R ) = ( 1.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 3.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 9.13e-10 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 8.03e-10 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 9.63e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 7.03e-10 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 2.04e-13 ) ; ( R ) = ( 2.83e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117612 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0197713 +Time: 5.64633e+07s, dt:154427s, Cycle: 962 +well_1Control: BHP (at the specified reference elevation): 46230521.62653274 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 8.21e-09 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.23e-03 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 8.82e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.01e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 4.82e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 5.05e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 3.22e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 6.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 9.14e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.75e-10 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.62e-04 ) ; ( Rwell ) = ( 1.81e-14 ) ; ( R ) = ( 1.62e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0197539 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.66177e+07s, dt:77213.3s, Cycle: 963 +well_1Control: BHP (at the specified reference elevation): 46275043.490025796 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 8.20e-09 ) ; ( R ) = ( 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 9.87e-10 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 7.59e-10 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.92e-10 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 4.82e-11 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 8.11e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 6.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.61e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.13e-06 ) ; ( Rwell ) = ( 5.15e-15 ) ; ( R ) = ( 4.13e-06 ) ; + Last LinSolve(iter,res) = ( 8, 5.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0586383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00983992 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.66949e+07s, dt:154427s, Cycle: 964 +well_1Control: BHP (at the specified reference elevation): 46297312.37087722 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 8.18e-09 ) ; ( R ) = ( 1.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 7.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 7.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 6.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 6.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 4.67e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 5.71e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.73e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 8.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.00e-04 ) ; ( Rwell ) = ( 8.00e-12 ) ; ( R ) = ( 2.00e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0196967 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.68493e+07s, dt:77213.3s, Cycle: 965 +well_1Control: BHP (at the specified reference elevation): 46341703.31222664 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 8.14e-09 ) ; ( R ) = ( 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 9.71e-10 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 2.51e-10 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.51e-05 ) ; ( Rwell ) = ( 1.20e-14 ) ; ( R ) = ( 7.51e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0585038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.010005 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.69266e+07s, dt:73440.9s, Cycle: 966 +well_1Control: BHP (at the specified reference elevation): 46363915.42353465 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 8.13e-09 ) ; ( R ) = ( 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 8.86e-10 ) ; ( R ) = ( 9.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 2.24e-10 ) ; ( R ) = ( 6.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.64e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.45e-05 ) ; ( Rwell ) = ( 5.81e-14 ) ; ( R ) = ( 2.45e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0556033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00961369 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.7e+07s, dt:146882s, Cycle: 967 +well_1Control: BHP (at the specified reference elevation): 46385030.84927848 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 8.12e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 8.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 9.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 6.67e-10 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.40e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 8.63e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.49e-10 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.54e-05 ) ; ( Rwell ) = ( 6.21e-15 ) ; ( R ) = ( 8.54e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.06e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46427170.15853896 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.111103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0190319 +compflowStatistics, reservoir: Pressure (min, average, max): 2.72188e+07, 2.72592e+07, 2.73692e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.46889e+07, 1.48393e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.463 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 22.4548, 717.008 } rm^3 +compflowStatistics, reservoir: Phase mass: { 14529.6, 700162 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2085.15, 216696 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 12444.5, 483466 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.5483, 8.08678 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 14510.1, 700154 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 14529.6, 0 }, { 2367.03, 697735 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.70051e+07, 2.71566e+07, 2.72374e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.44751e+07, 1.47075e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.908 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.908 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220425 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66127.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154297 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220425 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28433e-08, 220425 } } kg +compflowStatistics: Max phase CFL number: 286.559 +compflowStatistics: Max component CFL number: 393.782 +Time: 5.71469e+07s, dt:146882s, Cycle: 968 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 8.09e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.91e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.76e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 9.16e-10 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.98e-03 ) ; ( Rwell ) = ( 2.31e-10 ) ; ( R ) = ( 8.98e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.15e-04 ) ; ( Rwell ) = ( 1.04e-13 ) ; ( R ) = ( 1.15e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.110937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0191214 +Time: 5.72938e+07s, dt:146882s, Cycle: 969 +well_1Control: BHP (at the specified reference elevation): 46469292.891371414 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 8.07e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.98e-10 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.56e-05 ) ; ( Rwell ) = ( 1.20e-13 ) ; ( R ) = ( 4.56e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46511381.08561294 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.110773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0192916 +Time: 5.74406e+07s, dt:146882s, Cycle: 970 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 8.04e-09 ) ; ( R ) = ( 1.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 3.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 8.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 5.87e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.98e-04 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.98e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.11061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0188967 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.75875e+07s, dt:73440.9s, Cycle: 971 +well_1Control: BHP (at the specified reference elevation): 46553439.68628132 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 8.02e-09 ) ; ( R ) = ( 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 8.66e-10 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 2.22e-10 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.80e-05 ) ; ( Rwell ) = ( 4.40e-15 ) ; ( R ) = ( 7.80e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0552359 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00935598 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.7661e+07s, dt:146882s, Cycle: 972 +well_1Control: BHP (at the specified reference elevation): 46574482.08057779 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 8.01e-09 ) ; ( R ) = ( 1.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 8.12e-09 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.83e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 6.65e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.84e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 6.07e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 5.93e-09 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 5.50e-09 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 5.42e-09 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 5.33e-09 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.12e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-04 ) ; ( Rwell ) = ( 1.89e-13 ) ; ( R ) = ( 1.33e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.110378 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.018751 +Time: 5.78078e+07s, dt:146882s, Cycle: 973 +well_1Control: BHP (at the specified reference elevation): 46616489.47883377 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 7.99e-09 ) ; ( R ) = ( 1.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 9.01e-10 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 7.93e-10 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 6.96e-10 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 6.13e-10 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 5.38e-10 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.36e-10 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 7.96e-14 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 9, 9.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.110227 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0186394 +Time: 5.79547e+07s, dt:45268.5s, Cycle: 974 +well_1Control: BHP (at the specified reference elevation): 46658464.43269575 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 7.96e-09 ) ; ( R ) = ( 3.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.30e-10 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 6.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 2.52e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 2.22e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 4.31e-11 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 7.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 7.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 9.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.20e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 7.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 9.24e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.10e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 7.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 8.67e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 8.13e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 7.62e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 3.80e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 5.71e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 6.67e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.33e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.00e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 5.83e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 6.25e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.12e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 4.69e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 5.47e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 5.86e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.93e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 4.39e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 5.13e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 5.49e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.71e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 2.74e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 4.12e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 4.81e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 5.15e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 1.48e-12 ) ; ( R ) = ( 8.83e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46671432.693891406 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0339325 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00576743 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.8e+07s, dt:22634.2s, Cycle: 975 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; ( R ) = ( 1.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 8.23e-11 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 4.65e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.56e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.77e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.56e-05 ) ; ( Rwell ) = ( 6.77e-15 ) ; ( R ) = ( 4.56e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46677919.88834594 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.016959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00289173 +compflowStatistics, reservoir: Pressure (min, average, max): 2.73969e+07, 2.74373e+07, 2.75474e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.48923e+07, 1.50428e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.593 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 22.7213, 716.871 } rm^3 +compflowStatistics, reservoir: Phase mass: { 14759.2, 700125 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2116.15, 216764 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 12643, 483360 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.9496, 8.23325 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 14739.2, 700117 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 14759.2, 0 }, { 2396.43, 697668 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.71835e+07, 2.73348e+07, 2.74155e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.46789e+07, 1.49109e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.948 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.948 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220492 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66147.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154344 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220492 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28579e-08, 220492 } } kg +compflowStatistics: Max phase CFL number: 43.9812 +compflowStatistics: Max component CFL number: 60.4363 +Time: 5.80226e+07s, dt:22634.2s, Cycle: 976 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.98e-09 ) ; ( R ) = ( 1.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 8.83e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.61e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.54e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.14e-05 ) ; ( Rwell ) = ( 4.51e-15 ) ; ( R ) = ( 6.14e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46684405.1254193 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0169558 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00289707 +Time: 5.80453e+07s, dt:22634.2s, Cycle: 977 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 8.22e-11 ) ; ( R ) = ( 4.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 4.64e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.09e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.60e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.79e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 6.51e-15 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00289931 +Time: 5.80679e+07s, dt:22634.2s, Cycle: 978 +well_1Control: BHP (at the specified reference elevation): 46690888.661359556 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.97e-09 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 8.28e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 4.69e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.13e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.64e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.23e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 9.04e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169499 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00289915 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.80905e+07s, dt:45268.5s, Cycle: 979 +well_1Control: BHP (at the specified reference elevation): 46697366.953198195 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 7.95e-09 ) ; ( R ) = ( 3.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.28e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.52e-10 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 6.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.22e-10 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 1.94e-10 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.04e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.33e-10 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.92e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.39e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.34e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.02e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 9.04e-11 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.25e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 7.95e-11 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.00e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 7.00e-11 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.15e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 6.14e-11 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.02e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.83e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 5.40e-11 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.00e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 4.74e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.87e-05 ) ; ( Rwell ) = ( 1.38e-14 ) ; ( R ) = ( 7.87e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0338932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00579118 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.81358e+07s, dt:22634.2s, Cycle: 980 +well_1Control: BHP (at the specified reference elevation): 46710306.3270119 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 8.25e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 4.65e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.08e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.59e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.78e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.44e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 1.08e-14 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00290196 +Time: 5.81584e+07s, dt:22634.2s, Cycle: 981 +well_1Control: BHP (at the specified reference elevation): 46716778.16255943 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 8.10e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 4.55e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.99e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.51e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 1.04e-14 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00290424 +Time: 5.81811e+07s, dt:22634.2s, Cycle: 982 +well_1Control: BHP (at the specified reference elevation): 46723249.21510493 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 8.14e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.74e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.57e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.78e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.45e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.64e-05 ) ; ( Rwell ) = ( 1.31e-14 ) ; ( R ) = ( 3.64e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169346 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00290515 +Time: 5.82037e+07s, dt:22634.2s, Cycle: 983 +well_1Control: BHP (at the specified reference elevation): 46729718.44102502 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 8.27e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.69e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.13e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.64e-11 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 1.91e-14 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00290301 +Time: 5.82263e+07s, dt:22634.2s, Cycle: 984 +well_1Control: BHP (at the specified reference elevation): 46736186.24397674 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 8.18e-11 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.66e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.10e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.64e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.83e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.16e-05 ) ; ( Rwell ) = ( 9.16e-15 ) ; ( R ) = ( 5.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.37e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46742653.18695088 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0169288 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00289839 +Time: 5.8249e+07s, dt:22634.2s, Cycle: 985 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 8.14e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.58e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.03e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.54e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.13e-05 ) ; ( Rwell ) = ( 9.10e-15 ) ; ( R ) = ( 3.13e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.016926 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00289004 +Time: 5.82716e+07s, dt:22634.2s, Cycle: 986 +well_1Control: BHP (at the specified reference elevation): 46749119.54521522 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 9.79e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 6.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.37e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.46e-05 ) ; ( Rwell ) = ( 6.99e-15 ) ; ( R ) = ( 3.46e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.19e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46755586.02423644 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0169231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00288009 +Time: 5.82942e+07s, dt:22634.2s, Cycle: 987 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.92e-09 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 8.08e-11 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.55e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.00e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.52e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.72e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 9.70e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 1.22e-14 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0028789 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.83169e+07s, dt:11317.1s, Cycle: 988 +well_1Control: BHP (at the specified reference elevation): 46762052.14007737 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 7.92e-09 ) ; ( R ) = ( 9.03e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.19e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.94e-05 ) ; ( Rwell ) = ( 4.55e-15 ) ; ( R ) = ( 1.94e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845876 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143953 +Time: 5.83282e+07s, dt:11317.1s, Cycle: 989 +well_1Control: BHP (at the specified reference elevation): 46765285.003166735 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 7.91e-09 ) ; ( R ) = ( 9.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 6.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 9.69e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.12e-06 ) ; ( Rwell ) = ( 8.32e-16 ) ; ( R ) = ( 9.12e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845812 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143937 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.83395e+07s, dt:5658.56s, Cycle: 990 +well_1Control: BHP (at the specified reference elevation): 46768515.44629625 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; ( R ) = ( 4.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46770127.345043145 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00422933 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000719652 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.83452e+07s, dt:11317.1s, Cycle: 991 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 9.98e-12 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 8.82e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 7.79e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.89e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.19e-05 ) ; ( Rwell ) = ( 4.27e-15 ) ; ( R ) = ( 2.19e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0084598 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143839 +Time: 5.83565e+07s, dt:11317.1s, Cycle: 992 +well_1Control: BHP (at the specified reference elevation): 46773356.07200069 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; ( R ) = ( 9.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 9.43e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 8.10e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.15e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.03e-06 ) ; ( Rwell ) = ( 1.06e-15 ) ; ( R ) = ( 8.03e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0084565 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143749 +Time: 5.83678e+07s, dt:11317.1s, Cycle: 993 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 46776585.02315515 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; ( R ) = ( 9.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 8.02e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.27e-05 ) ; ( Rwell ) = ( 2.68e-15 ) ; ( R ) = ( 1.27e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.97e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46779813.47346474 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0084556 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143627 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.83791e+07s, dt:5658.56s, Cycle: 994 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 7.89e-09 ) ; ( R ) = ( 4.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00422768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000717851 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.83848e+07s, dt:11317.1s, Cycle: 995 +well_1Control: BHP (at the specified reference elevation): 46781425.6908406 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.87e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.89e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 1.64e-15 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46784651.76004429 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00845782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143392 +Time: 5.83961e+07s, dt:11317.1s, Cycle: 996 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 9.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 9.17e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.13e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.10e-05 ) ; ( Rwell ) = ( 4.35e-15 ) ; ( R ) = ( 2.10e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845365 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143211 +Time: 5.84074e+07s, dt:11317.1s, Cycle: 997 +well_1Control: BHP (at the specified reference elevation): 46787879.984494336 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 9.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.79e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.33e-05 ) ; ( Rwell ) = ( 3.75e-16 ) ; ( R ) = ( 2.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845273 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143041 +Time: 5.84187e+07s, dt:11317.1s, Cycle: 998 +well_1Control: BHP (at the specified reference elevation): 46791108.35095356 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 8.99e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.36e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 8.56e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 2.44e-15 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845192 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142856 +Time: 5.84301e+07s, dt:11317.1s, Cycle: 999 +well_1Control: BHP (at the specified reference elevation): 46794336.395918965 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 8.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 9.84e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.74e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.69e-05 ) ; ( Rwell ) = ( 9.43e-16 ) ; ( R ) = ( 1.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845113 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142644 +Time: 5.84414e+07s, dt:11317.1s, Cycle: 1000 +well_1Control: BHP (at the specified reference elevation): 46797564.050446495 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 8.97e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.13e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 2.89e-15 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845035 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142412 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.84527e+07s, dt:5658.56s, Cycle: 1001 +well_1Control: BHP (at the specified reference elevation): 46800791.724680245 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 4.48e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 7.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00422489 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000711512 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.84583e+07s, dt:11317.1s, Cycle: 1002 +well_1Control: BHP (at the specified reference elevation): 46802402.63539851 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.81e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.62e-05 ) ; ( Rwell ) = ( 3.59e-15 ) ; ( R ) = ( 2.62e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00845185 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142031 +Time: 5.84697e+07s, dt:11317.1s, Cycle: 1003 +well_1Control: BHP (at the specified reference elevation): 46805629.3893563 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 8.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 9.55e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 6.38e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.54e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.14e-05 ) ; ( Rwell ) = ( 2.76e-16 ) ; ( R ) = ( 1.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844847 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014205 +Time: 5.8481e+07s, dt:11317.1s, Cycle: 1004 +well_1Control: BHP (at the specified reference elevation): 46808856.58183293 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 8.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 8.41e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 7.41e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 7.43e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.91e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.25e-05 ) ; ( Rwell ) = ( 4.29e-15 ) ; ( R ) = ( 3.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142024 +Time: 5.84923e+07s, dt:11317.1s, Cycle: 1005 +well_1Control: BHP (at the specified reference elevation): 46812084.3567785 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 8.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.89e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.47e-05 ) ; ( Rwell ) = ( 2.51e-15 ) ; ( R ) = ( 1.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844679 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141986 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.85036e+07s, dt:5658.56s, Cycle: 1006 +well_1Control: BHP (at the specified reference elevation): 46815312.36904256 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 4.45e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 8.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00422353 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000709921 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.85093e+07s, dt:11317.1s, Cycle: 1007 +well_1Control: BHP (at the specified reference elevation): 46816923.42850751 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 9.45e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 8.34e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 3.87e-15 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141867 +Time: 5.85206e+07s, dt:11317.1s, Cycle: 1008 +well_1Control: BHP (at the specified reference elevation): 46820148.774328865 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 7.87e-09 ) ; ( R ) = ( 8.90e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.57e-05 ) ; ( Rwell ) = ( 2.52e-15 ) ; ( R ) = ( 1.57e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844505 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141747 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.85319e+07s, dt:5658.56s, Cycle: 1009 +well_1Control: BHP (at the specified reference elevation): 46823375.48940817 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-04 ) ; ( Rwell ) = ( 7.88e-09 ) ; ( R ) = ( 4.45e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 8.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0042224 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000708627 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.85376e+07s, dt:11317.1s, Cycle: 1010 +well_1Control: BHP (at the specified reference elevation): 46824985.71634352 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.86e-09 ) ; ( R ) = ( 1.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 9.67e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 5.84e-15 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.008448 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00141767 +Time: 5.85489e+07s, dt:11317.1s, Cycle: 1011 +well_1Control: BHP (at the specified reference elevation): 46828210.2624549 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 7.87e-09 ) ; ( R ) = ( 8.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 9.16e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 8.09e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.54e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 1.88e-15 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844323 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142256 +Time: 5.85602e+07s, dt:11317.1s, Cycle: 1012 +well_1Control: BHP (at the specified reference elevation): 46831436.808047086 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 7.87e-09 ) ; ( R ) = ( 8.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.91e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 7.12e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.89e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.69e-05 ) ; ( Rwell ) = ( 1.54e-15 ) ; ( R ) = ( 1.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.61e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46834663.224957675 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00844203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00142707 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.85715e+07s, dt:5658.56s, Cycle: 1013 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 7.87e-09 ) ; ( R ) = ( 4.44e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-04 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 8.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46836273.04612324 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00422107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000714864 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.85772e+07s, dt:11317.1s, Cycle: 1014 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 1.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 9.69e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.54e-05 ) ; ( Rwell ) = ( 9.29e-15 ) ; ( R ) = ( 2.54e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143367 +Time: 5.85885e+07s, dt:11317.1s, Cycle: 1015 +well_1Control: BHP (at the specified reference elevation): 46839493.727927476 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 8.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.49e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 8.37e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.80e-05 ) ; ( Rwell ) = ( 2.18e-15 ) ; ( R ) = ( 1.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00143741 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.85998e+07s, dt:5658.56s, Cycle: 1016 +well_1Control: BHP (at the specified reference elevation): 46842716.15515053 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 4.47e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 8.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46844325.12845701 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00422032 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000719783 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.86055e+07s, dt:11317.1s, Cycle: 1017 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 1.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 7.98e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 7.01e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.56e-05 ) ; ( Rwell ) = ( 2.78e-15 ) ; ( R ) = ( 1.56e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00844204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144237 +Time: 5.86168e+07s, dt:11317.1s, Cycle: 1018 +well_1Control: BHP (at the specified reference elevation): 46847545.58462757 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 8.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 8.84e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.10e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 9.13e-06 ) ; ( Rwell ) = ( 7.74e-16 ) ; ( R ) = ( 9.13e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00843821 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144523 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.86281e+07s, dt:5658.56s, Cycle: 1019 +well_1Control: BHP (at the specified reference elevation): 46850767.72634159 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 4.50e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00421944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000723322 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.86338e+07s, dt:11317.1s, Cycle: 1020 +well_1Control: BHP (at the specified reference elevation): 46852375.47202183 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; ( R ) = ( 1.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 9.33e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.21e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.73e-06 ) ; ( Rwell ) = ( 4.71e-15 ) ; ( R ) = ( 8.73e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46855597.67226952 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00843879 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00144893 +Time: 5.86451e+07s, dt:11317.1s, Cycle: 1021 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 9.03e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 9.95e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.78e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.33e-06 ) ; ( Rwell ) = ( 9.27e-16 ) ; ( R ) = ( 7.33e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00843586 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145117 +Time: 5.86564e+07s, dt:11317.1s, Cycle: 1022 +well_1Control: BHP (at the specified reference elevation): 46858820.245873675 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 9.05e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.21e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.85e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 3.78e-15 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46862042.736964226 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00843487 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145287 +Time: 5.86677e+07s, dt:11317.1s, Cycle: 1023 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 9.07e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 8.99e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.99e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.45e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.94e-06 ) ; ( Rwell ) = ( 3.02e-15 ) ; ( R ) = ( 6.94e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.008434 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014539 +Time: 5.8679e+07s, dt:11317.1s, Cycle: 1024 +well_1Control: BHP (at the specified reference elevation): 46865265.01605305 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 9.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.98e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 7.92e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.66e-06 ) ; ( Rwell ) = ( 1.01e-15 ) ; ( R ) = ( 7.66e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46868486.7690143 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00843313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145496 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.86903e+07s, dt:5658.56s, Cycle: 1025 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 4.55e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 8.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00421652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00072788 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.8696e+07s, dt:11317.1s, Cycle: 1026 +well_1Control: BHP (at the specified reference elevation): 46870096.18465034 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 7.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 8.20e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.21e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.35e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.37e-05 ) ; ( Rwell ) = ( 2.02e-15 ) ; ( R ) = ( 1.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00843522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145637 +Time: 5.87073e+07s, dt:11317.1s, Cycle: 1027 +well_1Control: BHP (at the specified reference elevation): 46873314.65373616 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 9.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.84e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.42e-05 ) ; ( Rwell ) = ( 1.20e-17 ) ; ( R ) = ( 1.42e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00843118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145688 +Time: 5.87186e+07s, dt:11317.1s, Cycle: 1028 +well_1Control: BHP (at the specified reference elevation): 46876535.16749899 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 9.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 7.82e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.89e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.07e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 3.18e-15 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00843011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145698 +Time: 5.873e+07s, dt:11317.1s, Cycle: 1029 +well_1Control: BHP (at the specified reference elevation): 46879755.93309957 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 9.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.99e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.84e-05 ) ; ( Rwell ) = ( 2.82e-15 ) ; ( R ) = ( 1.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842922 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00145673 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.87413e+07s, dt:5658.56s, Cycle: 1030 +well_1Control: BHP (at the specified reference elevation): 46882976.51412606 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 4.56e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 9.10e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46884584.83794151 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00421459 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000729406 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.87469e+07s, dt:11317.1s, Cycle: 1031 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.82e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 8.55e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.95e-05 ) ; ( Rwell ) = ( 3.05e-15 ) ; ( R ) = ( 2.95e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0084321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146256 +Time: 5.87582e+07s, dt:11317.1s, Cycle: 1032 +well_1Control: BHP (at the specified reference elevation): 46887801.38873783 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 7.82e-09 ) ; ( R ) = ( 9.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 9.45e-16 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842742 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146618 +Time: 5.87696e+07s, dt:11317.1s, Cycle: 1033 +well_1Control: BHP (at the specified reference elevation): 46891020.3446158 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 9.14e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 8.37e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.34e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.95e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.82e-05 ) ; ( Rwell ) = ( 1.19e-15 ) ; ( R ) = ( 1.82e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.72e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46894239.53326218 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0084262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014696 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.87809e+07s, dt:5658.56s, Cycle: 1034 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 4.58e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 9.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00421354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000735517 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.87865e+07s, dt:11317.1s, Cycle: 1035 +well_1Control: BHP (at the specified reference elevation): 46895846.34076293 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.81e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 7.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 6.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 8.80e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.18e-06 ) ; ( Rwell ) = ( 5.43e-16 ) ; ( R ) = ( 8.18e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842876 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147391 +Time: 5.87979e+07s, dt:11317.1s, Cycle: 1036 +well_1Control: BHP (at the specified reference elevation): 46899062.967195675 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 7.82e-09 ) ; ( R ) = ( 9.20e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 9.60e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 8.52e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.56e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.03e-05 ) ; ( Rwell ) = ( 1.67e-15 ) ; ( R ) = ( 2.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842435 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014748 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.88092e+07s, dt:5658.56s, Cycle: 1037 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 46902281.28475863 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 4.60e-04 ) ; ( Rwell ) = ( 7.83e-09 ) ; ( R ) = ( 4.60e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 5.45e-12 ) ; ( R ) = ( 9.41e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46903886.54606804 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00421237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000737885 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.88148e+07s, dt:11317.1s, Cycle: 1038 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.80e-09 ) ; ( R ) = ( 1.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 9.40e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 7.29e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 5.54e-15 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842456 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147617 +Time: 5.88261e+07s, dt:11317.1s, Cycle: 1039 +well_1Control: BHP (at the specified reference elevation): 46907102.93741864 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 7.81e-09 ) ; ( R ) = ( 9.23e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.93e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 5.64e-16 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147788 +Time: 5.88375e+07s, dt:11317.1s, Cycle: 1040 +well_1Control: BHP (at the specified reference elevation): 46910317.831818625 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 7.80e-09 ) ; ( R ) = ( 9.24e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.00e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.22e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.50e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.20e-05 ) ; ( Rwell ) = ( 2.94e-15 ) ; ( R ) = ( 2.20e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46913531.95360653 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00842124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147899 +Time: 5.88488e+07s, dt:11317.1s, Cycle: 1041 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 7.80e-09 ) ; ( R ) = ( 9.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.89e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.05e-05 ) ; ( Rwell ) = ( 3.69e-15 ) ; ( R ) = ( 2.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147995 +Time: 5.88601e+07s, dt:11317.1s, Cycle: 1042 +well_1Control: BHP (at the specified reference elevation): 46916746.14219435 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.39e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 8.31e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 7.10e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.33e-05 ) ; ( Rwell ) = ( 1.18e-15 ) ; ( R ) = ( 1.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841928 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148038 +Time: 5.88714e+07s, dt:11317.1s, Cycle: 1043 +well_1Control: BHP (at the specified reference elevation): 46919960.30498053 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 7.79e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.08e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.37e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.00e-05 ) ; ( Rwell ) = ( 6.29e-17 ) ; ( R ) = ( 1.00e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841833 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148041 +Time: 5.88827e+07s, dt:11317.1s, Cycle: 1044 +well_1Control: BHP (at the specified reference elevation): 46923174.81207149 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.82e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 7.76e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.84e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.82e-05 ) ; ( Rwell ) = ( 2.37e-15 ) ; ( R ) = ( 1.82e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.29e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46926389.15026297 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00841739 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148008 +Time: 5.88941e+07s, dt:11317.1s, Cycle: 1045 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 8.66e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 7.61e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.28e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.46e-05 ) ; ( Rwell ) = ( 1.35e-15 ) ; ( R ) = ( 2.46e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46929602.904243045 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00841644 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147942 +Time: 5.89054e+07s, dt:11317.1s, Cycle: 1046 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.03e-05 ) ; ( Rwell ) = ( 1.32e-15 ) ; ( R ) = ( 2.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.18e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46932816.31088443 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00841551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147882 +Time: 5.89167e+07s, dt:11317.1s, Cycle: 1047 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.90e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 4.06e-15 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014775 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.8928e+07s, dt:5658.56s, Cycle: 1048 +well_1Control: BHP (at the specified reference elevation): 46936029.28193587 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 4.64e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 5.85e-12 ) ; ( R ) = ( 9.62e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46937629.986993685 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00420748 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000738378 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.89337e+07s, dt:11317.1s, Cycle: 1049 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 7.76e-09 ) ; ( R ) = ( 1.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 7.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 5.99e-15 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147474 +Time: 5.8945e+07s, dt:11317.1s, Cycle: 1050 +well_1Control: BHP (at the specified reference elevation): 46940843.893535234 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 9.86e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 8.93e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.63e-06 ) ; ( Rwell ) = ( 1.52e-15 ) ; ( R ) = ( 9.63e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147298 +Time: 5.89563e+07s, dt:11317.1s, Cycle: 1051 +well_1Control: BHP (at the specified reference elevation): 46944056.9019417 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 9.91e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 6.76e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 2.37e-15 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147057 +Time: 5.89676e+07s, dt:11317.1s, Cycle: 1052 +well_1Control: BHP (at the specified reference elevation): 46947269.52967811 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 9.67e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 7.46e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.90e-05 ) ; ( Rwell ) = ( 1.16e-15 ) ; ( R ) = ( 1.90e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46950481.79744673 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00841026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146793 +Time: 5.89789e+07s, dt:11317.1s, Cycle: 1053 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 7.79e-09 ) ; ( R ) = ( 9.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 9.78e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 8.59e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.50e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.94e-05 ) ; ( Rwell ) = ( 7.25e-16 ) ; ( R ) = ( 1.94e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.96e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46953693.501942605 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0084093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146489 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.89902e+07s, dt:5658.56s, Cycle: 1054 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 7.78e-09 ) ; ( R ) = ( 4.62e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 7.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0042043 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000731788 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.89959e+07s, dt:4093.2s, Cycle: 1055 +well_1Control: BHP (at the specified reference elevation): 46955296.33275377 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 7.77e-09 ) ; ( R ) = ( 5.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 8.72e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00304847 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000528917 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.9e+07s, dt:8186.4s, Cycle: 1056 +well_1Control: BHP (at the specified reference elevation): 46956456.16339399 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; ( R ) = ( 1.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 7.45e-17 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.17e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46958777.59605774 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00608628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105588 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.75972e+07, 2.76376e+07, 2.77479e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.50955e+07, 1.52462e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.738 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 23.0219, 716.716 } rm^3 +compflowStatistics, reservoir: Phase mass: { 15018.5, 700082 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2149.97, 216842 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 12868.6, 483240 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.9844, 8.45461 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 14998.5, 700074 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 15018.5, 0 }, { 2428.47, 697592 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.73842e+07, 2.75353e+07, 2.76158e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.48825e+07, 1.51142e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 225.992 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 225.992 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220568 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66170.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154397 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220568 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28951e-08, 220568 } } kg +compflowStatistics: Max phase CFL number: 15.8367 +compflowStatistics: Max component CFL number: 21.7612 +Time: 5.90082e+07s, dt:16372.8s, Cycle: 1057 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; ( R ) = ( 1.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 9.01e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.52e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 6.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 9.99e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 8.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 6.97e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.16e-05 ) ; ( Rwell ) = ( 1.21e-15 ) ; ( R ) = ( 2.16e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00210396 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.90246e+07s, dt:8186.4s, Cycle: 1058 +well_1Control: BHP (at the specified reference elevation): 46963423.362824135 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 7.78e-09 ) ; ( R ) = ( 6.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 9.72e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 9.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46965744.44936196 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00607931 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105437 +Time: 5.90327e+07s, dt:8186.4s, Cycle: 1059 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 7.77e-09 ) ; ( R ) = ( 9.83e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 7.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 9.34e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 8.24e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 6.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.96e-06 ) ; ( Rwell ) = ( 2.44e-15 ) ; ( R ) = ( 7.96e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105694 +Time: 5.90409e+07s, dt:8186.4s, Cycle: 1060 +well_1Control: BHP (at the specified reference elevation): 46968067.722442165 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 7.78e-09 ) ; ( R ) = ( 6.63e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 8.39e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 7.41e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 5.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.54e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.87e-05 ) ; ( Rwell ) = ( 6.62e-16 ) ; ( R ) = ( 1.87e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.11e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46970391.14100787 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00607936 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105951 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.90491e+07s, dt:4093.2s, Cycle: 1061 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-04 ) ; ( Rwell ) = ( 7.78e-09 ) ; ( R ) = ( 3.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46971551.41471604 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00304063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000530456 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.90532e+07s, dt:8186.4s, Cycle: 1062 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 7.77e-09 ) ; ( R ) = ( 1.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.79e-05 ) ; ( Rwell ) = ( 1.50e-15 ) ; ( R ) = ( 2.79e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060817 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106309 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.90614e+07s, dt:16372.8s, Cycle: 1063 +well_1Control: BHP (at the specified reference elevation): 46973873.01229268 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.78e-09 ) ; ( R ) = ( 1.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 4.17e-11 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 3.22e-11 ) ; ( R ) = ( 6.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 2.83e-11 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 6.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.39e-12 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.48e-05 ) ; ( Rwell ) = ( 2.17e-15 ) ; ( R ) = ( 1.48e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46978513.594470814 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0121561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00213461 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.90778e+07s, dt:8186.4s, Cycle: 1064 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 6.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.86e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.66e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.47e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.32e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.21e-05 ) ; ( Rwell ) = ( 1.53e-16 ) ; ( R ) = ( 1.21e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060771 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0010692 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.9086e+07s, dt:4093.2s, Cycle: 1065 +well_1Control: BHP (at the specified reference elevation): 46980833.90025167 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.33e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 3.33e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.86e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 1.41e-12 ) ; ( R ) = ( 6.04e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.84e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46981992.24859042 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00303881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000535056 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.90901e+07s, dt:8186.4s, Cycle: 1066 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 1.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.00e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.10e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.54e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.33e-05 ) ; ( Rwell ) = ( 1.20e-15 ) ; ( R ) = ( 1.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46984313.0088043 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00607724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107183 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.90982e+07s, dt:4093.2s, Cycle: 1067 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 3.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 8.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46985470.98597948 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00303858 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000536499 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.91023e+07s, dt:8186.4s, Cycle: 1068 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; ( R ) = ( 1.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.15e-06 ) ; ( Rwell ) = ( 3.41e-15 ) ; ( R ) = ( 6.15e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00607783 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107415 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.91105e+07s, dt:16372.8s, Cycle: 1069 +well_1Control: BHP (at the specified reference elevation): 46987791.137156695 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 1.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 4.27e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 9.84e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 8.68e-12 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 7.66e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.52e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.13e-05 ) ; ( Rwell ) = ( 5.79e-16 ) ; ( R ) = ( 3.13e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.27e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46992431.1067445 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0121497 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00215345 +Time: 5.91269e+07s, dt:16372.8s, Cycle: 1070 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 1.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 4.25e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 4.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 9.65e-12 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.82e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 1.44e-15 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46997070.846002385 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0121474 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00215739 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.91433e+07s, dt:8186.4s, Cycle: 1071 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 6.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 6.94e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.50e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 6.50e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.45e-03 ) ; ( Rwell ) = ( 8.93e-12 ) ; ( R ) = ( 5.45e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.44e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.12e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.91e-13 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 8.77e-13 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 7.76e-13 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 46999389.34005602 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00607258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107949 +Time: 5.91514e+07s, dt:8186.4s, Cycle: 1072 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 9.39e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.30e-05 ) ; ( Rwell ) = ( 9.89e-16 ) ; ( R ) = ( 2.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47001709.433219664 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00607269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108015 +Time: 5.91596e+07s, dt:8186.4s, Cycle: 1073 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 6.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 8.20e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.83e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.64e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.46e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 3.81e-15 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.69e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47004029.6065439 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00607169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108077 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.91678e+07s, dt:4093.2s, Cycle: 1074 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 3.39e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 8.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00303633 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000540569 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.91719e+07s, dt:8186.4s, Cycle: 1075 +well_1Control: BHP (at the specified reference elevation): 47005187.323398195 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; ( R ) = ( 1.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.40e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.24e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.58e-05 ) ; ( Rwell ) = ( 2.52e-16 ) ; ( R ) = ( 1.58e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00607262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108131 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.91801e+07s, dt:16372.8s, Cycle: 1076 +well_1Control: BHP (at the specified reference elevation): 47007507.834055334 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 4.26e-11 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 6.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 5.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 9.38e-12 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.49e-05 ) ; ( Rwell ) = ( 5.22e-15 ) ; ( R ) = ( 2.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.35e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47012147.671748735 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0121404 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00216302 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.91965e+07s, dt:8186.4s, Cycle: 1077 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 6.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.19e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.19e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.39e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.94e-05 ) ; ( Rwell ) = ( 1.65e-15 ) ; ( R ) = ( 1.94e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108147 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.92047e+07s, dt:4093.2s, Cycle: 1078 +well_1Control: BHP (at the specified reference elevation): 47014467.75728218 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 3.39e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 9.05e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47015625.87299122 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00303516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000540757 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.92088e+07s, dt:8186.4s, Cycle: 1079 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; ( R ) = ( 1.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-05 ) ; ( Rwell ) = ( 8.40e-16 ) ; ( R ) = ( 1.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47017945.45834154 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00606993 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00108101 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.92169e+07s, dt:16372.8s, Cycle: 1080 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 4.21e-11 ) ; ( R ) = ( 7.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 3.23e-11 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.70e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.26e-05 ) ; ( Rwell ) = ( 3.53e-15 ) ; ( R ) = ( 3.26e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00216008 +Time: 5.92333e+07s, dt:16372.8s, Cycle: 1081 +well_1Control: BHP (at the specified reference elevation): 47022584.04673068 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 4.29e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 7.49e-12 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.60e-05 ) ; ( Rwell ) = ( 6.13e-15 ) ; ( R ) = ( 2.60e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47027223.05204212 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0121335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00215713 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.92497e+07s, dt:8186.4s, Cycle: 1082 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 6.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 8.05e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.97e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.53e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.35e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.19e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.67e-05 ) ; ( Rwell ) = ( 6.87e-16 ) ; ( R ) = ( 1.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47029543.10242065 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00606585 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107761 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.92579e+07s, dt:4093.2s, Cycle: 1083 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 3.39e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 9.10e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00303358 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000538693 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.9262e+07s, dt:8186.4s, Cycle: 1084 +well_1Control: BHP (at the specified reference elevation): 47030701.77528478 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.85e-05 ) ; ( Rwell ) = ( 6.37e-16 ) ; ( R ) = ( 1.85e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0060669 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107594 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.92702e+07s, dt:16372.8s, Cycle: 1085 +well_1Control: BHP (at the specified reference elevation): 47033021.06693207 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 1.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 4.21e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 5.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 8.81e-12 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.26e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.07e-05 ) ; ( Rwell ) = ( 5.57e-15 ) ; ( R ) = ( 2.07e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121288 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00214644 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.92865e+07s, dt:8186.4s, Cycle: 1086 +well_1Control: BHP (at the specified reference elevation): 47037660.67867747 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 6.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 6.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 7.65e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.61e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 4.55e-17 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00606353 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00107163 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.92947e+07s, dt:4093.2s, Cycle: 1087 +well_1Control: BHP (at the specified reference elevation): 47039981.04527648 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-04 ) ; ( Rwell ) = ( 7.75e-09 ) ; ( R ) = ( 3.38e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 8.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47041138.7491347 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0030327 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00053561 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.92988e+07s, dt:8186.4s, Cycle: 1088 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 7.73e-09 ) ; ( R ) = ( 1.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.90e-05 ) ; ( Rwell ) = ( 2.17e-15 ) ; ( R ) = ( 1.90e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00606584 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106917 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.9307e+07s, dt:16372.8s, Cycle: 1089 +well_1Control: BHP (at the specified reference elevation): 47043458.478899285 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 7.74e-09 ) ; ( R ) = ( 1.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 4.06e-11 ) ; ( R ) = ( 6.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 6.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.85e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 5.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 6.05e-12 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.82e-05 ) ; ( Rwell ) = ( 2.58e-15 ) ; ( R ) = ( 2.82e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121244 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00213065 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.93234e+07s, dt:8186.4s, Cycle: 1090 +well_1Control: BHP (at the specified reference elevation): 47048093.85582113 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 7.72e-09 ) ; ( R ) = ( 6.73e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 8.58e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 7.58e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 5.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.83e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.64e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.51e-05 ) ; ( Rwell ) = ( 1.91e-15 ) ; ( R ) = ( 1.51e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00606134 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00106192 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.93315e+07s, dt:4093.2s, Cycle: 1091 +well_1Control: BHP (at the specified reference elevation): 47050411.52662738 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.36e-04 ) ; ( Rwell ) = ( 7.72e-09 ) ; ( R ) = ( 3.36e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 8.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00303144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000530519 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.93356e+07s, dt:8186.4s, Cycle: 1092 +well_1Control: BHP (at the specified reference elevation): 47051568.91670081 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; ( R ) = ( 1.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.41e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47053883.60223161 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00605825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00105869 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.93438e+07s, dt:16372.8s, Cycle: 1093 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.70e-09 ) ; ( R ) = ( 1.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 4.19e-11 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 5.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.15e-05 ) ; ( Rwell ) = ( 7.79e-15 ) ; ( R ) = ( 4.15e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00212053 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.93602e+07s, dt:32745.6s, Cycle: 1094 +well_1Control: BHP (at the specified reference elevation): 47058516.644852936 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; ( R ) = ( 2.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.66e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.27e-10 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.03e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 8.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 7.77e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 7.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.83e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-05 ) ; ( Rwell ) = ( 4.16e-15 ) ; ( R ) = ( 1.63e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47067781.14597851 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0242334 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00426134 +Time: 5.93929e+07s, dt:32745.6s, Cycle: 1095 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; ( R ) = ( 2.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 1.66e-10 ) ; ( R ) = ( 7.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 9.41e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.92e-05 ) ; ( Rwell ) = ( 1.19e-14 ) ; ( R ) = ( 4.92e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.04e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47077047.66077994 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0242249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00427407 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.94257e+07s, dt:65491.2s, Cycle: 1096 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 7.71e-09 ) ; ( R ) = ( 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 6.57e-10 ) ; ( R ) = ( 9.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 1.66e-10 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.20e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 8.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.35e-11 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.18e-06 ) ; ( Rwell ) = ( 1.61e-14 ) ; ( R ) = ( 5.18e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.38e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47095570.47663583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0484283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00854362 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.94912e+07s, dt:130982s, Cycle: 1097 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 7.70e-09 ) ; ( R ) = ( 1.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; ( R ) = ( 5.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 7.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.41e-03 ) ; ( Rwell ) = ( 6.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 3.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 9.20e-10 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 8.06e-10 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 7.12e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 6.29e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 5.54e-10 ) ; ( R ) = ( 6.42e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.21e-04 ) ; ( Rwell ) = ( 1.27e-14 ) ; ( R ) = ( 2.21e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47132533.0574752 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0967673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0166807 +Time: 5.96222e+07s, dt:130982s, Cycle: 1098 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 7.67e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.25e-03 ) ; ( Rwell ) = ( 6.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.91e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 9.89e-10 ) ; ( R ) = ( 3.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 8.70e-10 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 7.66e-10 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 6.73e-10 ) ; ( R ) = ( 8.34e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 7.25e-14 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0966267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.016654 +Time: 5.97531e+07s, dt:130982s, Cycle: 1099 +well_1Control: BHP (at the specified reference elevation): 47169483.33946107 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 7.65e-09 ) ; ( R ) = ( 1.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 8.66e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.18e-03 ) ; ( Rwell ) = ( 8.44e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.56e-03 ) ; ( Rwell ) = ( 9.02e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 7.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 7.46e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 8.06e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-03 ) ; ( Rwell ) = ( 8.50e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 9.78e-10 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 6.98e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.65e-03 ) ; ( Rwell ) = ( 7.59e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.25e-03 ) ; ( Rwell ) = ( 8.00e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.43e-03 ) ; ( Rwell ) = ( 8.66e-10 ) ; ( R ) = ( 8.43e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 6.17e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 2.19e-10 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 4.15e-14 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0964868 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.016657 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.98841e+07s, dt:115869s, Cycle: 1100 +well_1Control: BHP (at the specified reference elevation): 47206400.097699575 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 7.63e-09 ) ; ( R ) = ( 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 8.84e-10 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.70e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 7.75e-10 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 6.83e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.68e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.36e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 6.01e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.87e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 5.29e-10 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.64e-10 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 4.09e-10 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 3.59e-10 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.42e-04 ) ; ( Rwell ) = ( 9.36e-14 ) ; ( R ) = ( 2.42e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0852365 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0147906 +Time: 6e+07s, dt:115869s, Cycle: 1101 +well_1Control: BHP (at the specified reference elevation): 47239057.411987714 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.33e-03 ) ; ( Rwell ) = ( 7.62e-09 ) ; ( R ) = ( 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 9.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 6.90e-11 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.88e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 4.28e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-03 ) ; ( Rwell ) = ( 6.03e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 9.92e-10 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.18e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.68e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-03 ) ; ( Rwell ) = ( 3.72e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.67e-03 ) ; ( Rwell ) = ( 5.26e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 8.73e-10 ) ; ( R ) = ( 9.80e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 1.92e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.89e-05 ) ; ( Rwell ) = ( 1.66e-13 ) ; ( R ) = ( 6.89e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0851315 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0145159 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +well_1Control: BHP (at the specified reference elevation): 47271671.55128084 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.78213e+07, 2.78617e+07, 2.79721e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.52979e+07, 1.54487e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 739.901 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 23.3566, 716.544 } rm^3 +compflowStatistics, reservoir: Phase mass: { 15308.6, 700036 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2188.73, 216928 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 13119.9, 483108 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.0737, 9.49588 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 15288.6, 700026 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 15308.6, 0 }, { 2465.88, 697507 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.7609e+07, 2.77596e+07, 2.784e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.50856e+07, 1.53166e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.042 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.042 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220652 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66195.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154457 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220652 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.30541e-08, 220652 } } kg +compflowStatistics: Max phase CFL number: 223.059 +compflowStatistics: Max component CFL number: 306.496 +Time: 6.01159e+07s, dt:231738s, Cycle: 1102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 7.60e-09 ) ; ( R ) = ( 1.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 7.61e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 7.73e-10 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 2.68e-14 ) ; ( R ) = ( 6.51e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.169949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0286624 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.03476e+07s, dt:382212s, Cycle: 1103 +well_1Control: BHP (at the specified reference elevation): 47336655.69430603 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 7.55e-09 ) ; ( R ) = ( 2.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 7.52e-08 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 15, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 3.08e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.05e-05 ) ; ( Rwell ) = ( 2.38e-15 ) ; ( R ) = ( 3.05e-05 ) ; + Last LinSolve(iter,res) = ( 12, 9.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.279273 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0478204 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.07298e+07s, dt:270180s, Cycle: 1104 +well_1Control: BHP (at the specified reference elevation): 47443474.797310755 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 7.49e-09 ) ; ( R ) = ( 2.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 7.00e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 6.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 6.03e-09 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 5.34e-09 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 5.28e-02 ) ; + Last LinSolve(iter,res) = ( 10, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; ( R ) = ( 5.36e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 6.07e-10 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.98e-04 ) ; ( Rwell ) = ( 4.93e-13 ) ; ( R ) = ( 3.98e-04 ) ; + Last LinSolve(iter,res) = ( 11, 8.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.196695 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0324794 +Time: 6.1e+07s, dt:270180s, Cycle: 1105 +well_1Control: BHP (at the specified reference elevation): 47519143.790218845 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 7.47e-09 ) ; ( R ) = ( 2.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; ( R ) = ( 7.50e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 9.74e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 9.88e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 9.99e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 9.89e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 9.40e-09 ) ; ( R ) = ( 4.02e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 9.88e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 8.92e-09 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 9.77e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 8.51e-09 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 9.61e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 8.15e-09 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 9.40e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 7.82e-09 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 9.17e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 7.56e-09 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.23e-04 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 3.23e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.196204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0327796 +compflowStatistics, reservoir: Pressure (min, average, max): 2.80537e+07, 2.80941e+07, 2.82047e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.54993e+07, 1.56502e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.07 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 23.702, 716.368 } rm^3 +compflowStatistics, reservoir: Phase mass: { 15609.3, 699990 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2229.76, 217018 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 13379.5, 482972 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.4021, 9.98966 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 15588.9, 699980 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 15609.3, 0 }, { 2506.53, 697419 } } kg +well_1Control: BHP (at the specified reference elevation): 47594690.57773268 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.78423e+07, 2.79922e+07, 2.80724e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.52878e+07, 1.55179e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.094 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.094 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220740 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66222 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154518 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220740 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.41601e-08, 220740 } } kg +compflowStatistics: Max phase CFL number: 517.548 +compflowStatistics: Max component CFL number: 711.115 +Time: 6.12702e+07s, dt:270180s, Cycle: 1106 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 7.43e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; ( R ) = ( 6.73e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 9, 1.00e-02 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 9.74e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 9.85e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; ( R ) = ( 5.90e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 9.62e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 9, 1.00e-02 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 9.54e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 9.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 9.18e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 8.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 8.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 8.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.56e-04 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 2.56e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.195734 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0309777 +Time: 6.15404e+07s, dt:270180s, Cycle: 1107 +well_1Control: BHP (at the specified reference elevation): 47670108.23554293 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 7.39e-09 ) ; ( R ) = ( 1.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 9.73e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 9.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 9.89e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 9.85e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 9.74e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 9.56e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 9.35e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 4.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 5.49e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.09e-04 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 3.09e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.195258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0309911 +Time: 6.18105e+07s, dt:189460s, Cycle: 1108 +well_1Control: BHP (at the specified reference elevation): 47745373.6253241 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 7.34e-09 ) ; ( R ) = ( 1.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 6.82e-09 ) ; ( R ) = ( 6.66e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 6.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 5.67e-09 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 5.24e-09 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 4.83e-09 ) ; ( R ) = ( 4.23e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; ( R ) = ( 5.61e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 3.13e-13 ) ; ( R ) = ( 7.57e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.136626 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0218995 +Time: 6.2e+07s, dt:189460s, Cycle: 1109 +well_1Control: BHP (at the specified reference elevation): 47798185.74544096 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 7.33e-09 ) ; ( R ) = ( 1.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 5.04e-09 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 5.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 3.03e-09 ) ; ( R ) = ( 1.41e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.91e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 9.91e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 6.56e-10 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.62e-02 ) ; ( Rwell ) = ( 5.77e-10 ) ; ( R ) = ( 9.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 9.66e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 5.07e-10 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 9.12e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 4.46e-10 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.99e-04 ) ; ( Rwell ) = ( 4.21e-14 ) ; ( R ) = ( 2.99e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.85e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47850923.77794102 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.136419 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0220574 +compflowStatistics, reservoir: Pressure (min, average, max): 2.82388e+07, 2.82792e+07, 2.83899e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.57006e+07, 1.58517e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.205 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 23.978, 716.227 } rm^3 +compflowStatistics, reservoir: Phase mass: { 15850, 699952 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2261.4, 217090 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 13588.6, 482863 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.7118, 10.8996 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 15830.3, 699941 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 15850, 0 }, { 2537.58, 697350 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.80276e+07, 2.81774e+07, 2.82575e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.54894e+07, 1.57193e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.135 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.135 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220810 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66242.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154567 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220810 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.79511e-08, 220810 } } kg +compflowStatistics: Max phase CFL number: 361.517 +compflowStatistics: Max component CFL number: 496.711 +Time: 6.21895e+07s, dt:189460s, Cycle: 1110 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 7.30e-09 ) ; ( R ) = ( 1.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 3.69e-08 ) ; ( R ) = ( 2.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 7.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 6.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 6.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 9.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 5.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 6.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 5.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 5.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.43e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 8.43e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 7.75e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 3.50e-08 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.01e-13 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 9, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.93e-06 ) ; ( Rwell ) = ( 4.89e-16 ) ; ( R ) = ( 5.93e-06 ) ; + Last LinSolve(iter,res) = ( 11, 1.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.136209 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0224504 +Time: 6.23789e+07s, dt:189460s, Cycle: 1111 +well_1Control: BHP (at the specified reference elevation): 47903590.68009629 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 7.27e-09 ) ; ( R ) = ( 1.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.62e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; ( R ) = ( 2.91e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; ( R ) = ( 3.10e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 5.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 6.66e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 6.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 5.20e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 7.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 8.83e-10 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 7.76e-10 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 6.83e-10 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 9.75e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 4.44e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.33e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.27e-05 ) ; ( Rwell ) = ( 6.76e-15 ) ; ( R ) = ( 4.27e-05 ) ; + Last LinSolve(iter,res) = ( 11, 6.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.135991 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0224697 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.25684e+07s, dt:94729.8s, Cycle: 1112 +well_1Control: BHP (at the specified reference elevation): 47956186.628533915 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.12e-03 ) ; ( Rwell ) = ( 7.24e-09 ) ; ( R ) = ( 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 7.13e-10 ) ; ( R ) = ( 6.15e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.29e-03 ) ; ( Rwell ) = ( 1.79e-10 ) ; ( R ) = ( 7.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 3.98e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 3.99e-15 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.49e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 47982505.4572933 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855639e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0678969 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0113462 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.26631e+07s, dt:189460s, Cycle: 1113 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 7.23e-09 ) ; ( R ) = ( 1.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 3.11e-08 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 6.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 3.05e-08 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 6.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 5.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.44e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 8.44e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 6.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 7.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 8.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 8.03e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 5.81e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.18e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 5.10e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 6.79e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 7.47e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 4.87e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 4.79e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 6.33e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 6.95e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 6.29e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 4.50e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 5.91e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 6.47e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 1.00e-09 ) ; ( R ) = ( 4.81e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 7.26e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 4.23e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 5.51e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 6.03e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 8.82e-10 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 8.09e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 3.97e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 5.14e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 5.62e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 7.76e-10 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 8.69e-11 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.97e-10 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.73e-05 ) ; ( Rwell ) = ( 1.33e-13 ) ; ( R ) = ( 7.73e-05 ) ; + Last LinSolve(iter,res) = ( 10, 9.24e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48034983.13056642 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.135662 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0221255 +Time: 6.28526e+07s, dt:147431s, Cycle: 1114 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 7.20e-09 ) ; ( R ) = ( 1.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 6.19e-09 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.67e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 5.53e-09 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 5.26e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.86e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; ( R ) = ( 4.02e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 4.82e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.55e-05 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 4.55e-05 ) ; + Last LinSolve(iter,res) = ( 10, 6.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.1054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0169762 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.3e+07s, dt:73715.7s, Cycle: 1115 +well_1Control: BHP (at the specified reference elevation): 48075823.560919836 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; ( R ) = ( 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 7.51e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 4.24e-10 ) ; ( R ) = ( 8.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 3.25e-10 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 2.87e-10 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 2.54e-10 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 2.22e-10 ) ; ( R ) = ( 6.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 1.96e-10 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.27e-05 ) ; ( Rwell ) = ( 6.12e-14 ) ; ( R ) = ( 4.27e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0526396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00851103 +compflowStatistics, reservoir: Pressure (min, average, max): 2.84166e+07, 2.84571e+07, 2.85678e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.59018e+07, 1.6053e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.334 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 24.2435, 716.09 } rm^3 +compflowStatistics, reservoir: Phase mass: { 16082.1, 699915 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2291.66, 217158 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 13790.4, 482757 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.9391, 11.0388 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 16062.1, 699904 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 16082.1, 0 }, { 2566.99, 697283 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.82057e+07, 2.83553e+07, 2.84353e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.56909e+07, 1.59205e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.174 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.174 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220877 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66263 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154614 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220877 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 3.95959e-08, 220877 } } kg +well_1Control: BHP (at the specified reference elevation): 48096262.979180574 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 140.145 +compflowStatistics: Max component CFL number: 192.548 +Time: 6.30737e+07s, dt:73715.7s, Cycle: 1116 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 7.18e-09 ) ; ( R ) = ( 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 7.54e-10 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.70e-03 ) ; ( Rwell ) = ( 4.27e-10 ) ; ( R ) = ( 8.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 3.26e-10 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.85e-10 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.62e-10 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 1.42e-10 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 8.04e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.07e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.44e-05 ) ; ( Rwell ) = ( 1.43e-14 ) ; ( R ) = ( 3.44e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0526079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00852183 +Time: 6.31474e+07s, dt:73715.7s, Cycle: 1117 +well_1Control: BHP (at the specified reference elevation): 48116687.920630544 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 7.16e-09 ) ; ( R ) = ( 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 7.53e-10 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 1.90e-10 ) ; ( R ) = ( 6.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 1.67e-10 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 1.46e-10 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.05e-05 ) ; ( Rwell ) = ( 2.03e-14 ) ; ( R ) = ( 3.05e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0525767 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00846666 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.32211e+07s, dt:147431s, Cycle: 1118 +well_1Control: BHP (at the specified reference elevation): 48137109.708298236 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 7.16e-09 ) ; ( R ) = ( 1.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 2.47e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 2.90e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.42e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.38e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 4.88e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 2.71e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.31e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.29e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.39e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 2.53e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.20e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 3.22e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 3.95e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.36e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.10e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.10e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 3.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.00e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 2.01e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 8.88e-10 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.23e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.24e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.81e-05 ) ; ( Rwell ) = ( 1.00e-13 ) ; ( R ) = ( 5.81e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.105084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0173323 +Time: 6.33686e+07s, dt:147431s, Cycle: 1119 +well_1Control: BHP (at the specified reference elevation): 48177853.11776478 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 7.13e-09 ) ; ( R ) = ( 1.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 9.03e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.41e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 8.86e-09 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 8.71e-09 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 8.56e-09 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 8.43e-09 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 8.32e-09 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 8.21e-09 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 7.66e-09 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.99e-11 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 1.10e-10 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.47e-05 ) ; ( Rwell ) = ( 8.22e-14 ) ; ( R ) = ( 2.47e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.104952 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0172882 +Time: 6.3516e+07s, dt:147431s, Cycle: 1120 +well_1Control: BHP (at the specified reference elevation): 48218586.809089124 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 7.11e-09 ) ; ( R ) = ( 1.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 9.26e-10 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 8.14e-10 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 7.16e-10 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 4.04e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.56e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 3.13e-10 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 2.68e-13 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.97e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48259273.30274922 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.104819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0167773 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.36634e+07s, dt:73715.7s, Cycle: 1121 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 7.08e-09 ) ; ( R ) = ( 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.73e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 7.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 8.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; ( R ) = ( 6.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 6.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 6.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.21e-05 ) ; ( Rwell ) = ( 1.06e-12 ) ; ( R ) = ( 2.21e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48279640.24682359 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0523484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00835985 +Time: 6.37372e+07s, dt:73715.7s, Cycle: 1122 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 7.09e-09 ) ; ( R ) = ( 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 7.35e-10 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 4.17e-10 ) ; ( R ) = ( 8.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 2.35e-10 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 2.07e-10 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 1.82e-10 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 1.61e-10 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 1.42e-10 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.24e-10 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.10e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.41e-05 ) ; ( Rwell ) = ( 3.60e-14 ) ; ( R ) = ( 2.41e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.052317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00839752 +Time: 6.38109e+07s, dt:73715.7s, Cycle: 1123 +well_1Control: BHP (at the specified reference elevation): 48299989.00117808 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 7.07e-09 ) ; ( R ) = ( 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 7.40e-10 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.61e-03 ) ; ( Rwell ) = ( 4.17e-10 ) ; ( R ) = ( 8.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.02e-03 ) ; ( Rwell ) = ( 3.19e-10 ) ; ( R ) = ( 8.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.67e-03 ) ; ( Rwell ) = ( 2.81e-10 ) ; ( R ) = ( 7.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 2.48e-10 ) ; ( R ) = ( 6.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 2.18e-10 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.92e-10 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.82e-11 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.05e-06 ) ; ( Rwell ) = ( 4.43e-14 ) ; ( R ) = ( 8.05e-06 ) ; + Last LinSolve(iter,res) = ( 8, 5.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0522858 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00837217 +Time: 6.38846e+07s, dt:73715.7s, Cycle: 1124 +well_1Control: BHP (at the specified reference elevation): 48320329.67381427 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; ( R ) = ( 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 7.38e-10 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 4.17e-10 ) ; ( R ) = ( 8.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 3.20e-10 ) ; ( R ) = ( 7.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 2.81e-10 ) ; ( R ) = ( 6.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 2.47e-10 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 6.22e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.29e-05 ) ; ( Rwell ) = ( 1.04e-15 ) ; ( R ) = ( 3.29e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0522541 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00840085 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.39583e+07s, dt:41696.2s, Cycle: 1125 +well_1Control: BHP (at the specified reference elevation): 48340665.70300653 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; ( R ) = ( 3.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 4.65e-09 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; ( R ) = ( 7.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; ( R ) = ( 7.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; ( R ) = ( 6.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 8.87e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; ( R ) = ( 6.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 5.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; ( R ) = ( 5.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 2.46e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 4.53e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 3.18e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 5.44e-11 ) ; ( R ) = ( 4.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 4.74e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 4.17e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 9.37e-12 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 6.73e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 6.31e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 9.50e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.19e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 5.92e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 8.90e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.55e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 8.35e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 9.74e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 5.21e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 1.40e-12 ) ; ( R ) = ( 6.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00475135 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.4e+07s, dt:20848.1s, Cycle: 1126 +well_1Control: BHP (at the specified reference elevation): 48352177.25462682 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.88e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.84e-05 ) ; ( Rwell ) = ( 2.93e-15 ) ; ( R ) = ( 3.84e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.76e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48357935.39192146 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0147655 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00237348 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.86069e+07, 2.86474e+07, 2.87583e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.61028e+07, 1.62541e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.472 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 24.528, 715.944 } rm^3 +compflowStatistics, reservoir: Phase mass: { 16331.3, 699875 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2324.57, 217232 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 14006.7, 482644 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.0699, 11.0401 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 16311.2, 699864 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 16331.3, 0 }, { 2597.81, 697211 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.83963e+07, 2.85457e+07, 2.86256e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.58921e+07, 1.61214e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.217 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.217 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 220949 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66284.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154664 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 220949 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 7.83796e-08, 220949 } } kg +compflowStatistics: Max phase CFL number: 39.4824 +compflowStatistics: Max component CFL number: 54.2436 +Time: 6.40208e+07s, dt:41696.2s, Cycle: 1127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.06e-09 ) ; ( R ) = ( 3.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.66e-03 ) ; ( Rwell ) = ( 2.35e-10 ) ; ( R ) = ( 9.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.45e-03 ) ; ( Rwell ) = ( 1.18e-10 ) ; ( R ) = ( 5.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 1.04e-10 ) ; ( R ) = ( 6.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 9.11e-11 ) ; ( R ) = ( 6.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 8.05e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 7.09e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 6.21e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 5.45e-11 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 8.30e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.22e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 9.36e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.75e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 8.78e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.47e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.23e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.60e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.68e-06 ) ; ( Rwell ) = ( 4.77e-15 ) ; ( R ) = ( 9.68e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295268 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00473885 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.40625e+07s, dt:20848.1s, Cycle: 1128 +well_1Control: BHP (at the specified reference elevation): 48369433.452167556 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 6.02e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 8.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00237469 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.40834e+07s, dt:41696.2s, Cycle: 1129 +well_1Control: BHP (at the specified reference elevation): 48375179.393866286 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; ( R ) = ( 3.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 2.36e-10 ) ; ( R ) = ( 9.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.06e-03 ) ; ( Rwell ) = ( 1.33e-10 ) ; ( R ) = ( 8.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.39e-03 ) ; ( Rwell ) = ( 1.17e-10 ) ; ( R ) = ( 8.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.07e-03 ) ; ( Rwell ) = ( 6.63e-11 ) ; ( R ) = ( 7.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 5.83e-11 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 5.08e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 4.47e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.93e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.46e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.67e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.34e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.89e-06 ) ; ( Rwell ) = ( 1.09e-15 ) ; ( R ) = ( 8.89e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295122 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00476078 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.41251e+07s, dt:20848.1s, Cycle: 1130 +well_1Control: BHP (at the specified reference elevation): 48386673.92082973 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.98e-11 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00238137 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.41459e+07s, dt:41696.2s, Cycle: 1131 +well_1Control: BHP (at the specified reference elevation): 48392413.96108427 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; ( R ) = ( 3.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.13e-03 ) ; ( Rwell ) = ( 2.37e-10 ) ; ( R ) = ( 9.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 6.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 1.17e-10 ) ; ( R ) = ( 8.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.70e-03 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 7.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 9.08e-11 ) ; ( R ) = ( 7.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 7.99e-11 ) ; ( R ) = ( 7.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 7.03e-11 ) ; ( R ) = ( 6.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 6.18e-11 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 5.44e-11 ) ; ( R ) = ( 6.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 4.79e-11 ) ; ( R ) = ( 5.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 4.21e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 3.68e-11 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.23e-05 ) ; ( Rwell ) = ( 7.48e-15 ) ; ( R ) = ( 2.23e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0294975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00475528 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.41876e+07s, dt:20848.1s, Cycle: 1132 +well_1Control: BHP (at the specified reference elevation): 48403906.38839572 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 5.91e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.30e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.63e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.61e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.36e-05 ) ; ( Rwell ) = ( 9.22e-15 ) ; ( R ) = ( 5.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00238421 +Time: 6.42085e+07s, dt:20848.1s, Cycle: 1133 +well_1Control: BHP (at the specified reference elevation): 48409653.3949053 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.03e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.36e-10 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.10e-10 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.09e-10 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.06e-10 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.02e-10 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.00e-10 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.98e-10 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.93e-10 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.88e-10 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 8.91e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.85e-04 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 2.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00239121 +Time: 6.42293e+07s, dt:20848.1s, Cycle: 1134 +well_1Control: BHP (at the specified reference elevation): 48415396.33335511 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.84e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.85e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.37e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 6.48e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 9.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 8.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147359 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00239603 +Time: 6.42502e+07s, dt:20848.1s, Cycle: 1135 +well_1Control: BHP (at the specified reference elevation): 48421138.726339266 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.01e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 5.85e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.51e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.97e-11 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.49e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.36e-05 ) ; ( Rwell ) = ( 1.43e-14 ) ; ( R ) = ( 6.36e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147375 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00239992 +Time: 6.4271e+07s, dt:20848.1s, Cycle: 1136 +well_1Control: BHP (at the specified reference elevation): 48426882.45367107 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.02e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.86e-11 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 6.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014733 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240285 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.42919e+07s, dt:41696.2s, Cycle: 1137 +well_1Control: BHP (at the specified reference elevation): 48432618.199778065 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 3.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.09e-03 ) ; ( Rwell ) = ( 2.35e-10 ) ; ( R ) = ( 7.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 9.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 8.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.94e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 7.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 9.00e-11 ) ; ( R ) = ( 7.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 7.91e-11 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 6.96e-11 ) ; ( R ) = ( 6.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 3.96e-11 ) ; ( R ) = ( 4.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 3.49e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 2.35e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 1.10e-15 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.029465 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00482794 +Time: 6.43336e+07s, dt:41696.2s, Cycle: 1138 +well_1Control: BHP (at the specified reference elevation): 48444086.82022089 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 3.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 2.34e-10 ) ; ( R ) = ( 9.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 8.92e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 7.88e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 6.93e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.90e-03 ) ; ( Rwell ) = ( 6.10e-11 ) ; ( R ) = ( 7.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 8.75e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 6.56e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 7.66e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 8.21e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.55e-06 ) ; ( Rwell ) = ( 1.45e-15 ) ; ( R ) = ( 8.55e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0294547 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00484677 +Time: 6.43753e+07s, dt:41696.2s, Cycle: 1139 +well_1Control: BHP (at the specified reference elevation): 48455555.421635136 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 3.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 2.35e-10 ) ; ( R ) = ( 8.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 6.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 8.98e-11 ) ; ( R ) = ( 5.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 7.91e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 6.96e-11 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 6.13e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 5.35e-11 ) ; ( R ) = ( 5.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 4.70e-11 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 4.13e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 3.64e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 8.36e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 8.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 7.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 9.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 6.77e-05 ) ; ( Rwell ) = ( 1.91e-14 ) ; ( R ) = ( 6.77e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.029445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0048693 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.4417e+07s, dt:20848.1s, Cycle: 1140 +well_1Control: BHP (at the specified reference elevation): 48467026.74707602 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.84e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.94e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.20e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.13e-05 ) ; ( Rwell ) = ( 1.39e-14 ) ; ( R ) = ( 6.13e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.35e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48472765.505850345 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0147178 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244144 +Time: 6.44378e+07s, dt:20848.1s, Cycle: 1141 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 1.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 5.82e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.58e-05 ) ; ( Rwell ) = ( 4.62e-15 ) ; ( R ) = ( 4.58e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244652 +Time: 6.44587e+07s, dt:20848.1s, Cycle: 1142 +well_1Control: BHP (at the specified reference elevation): 48478503.656326056 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 1.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.91e-10 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.68e-10 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.59e-10 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 4.55e-10 ) ; ( R ) = ( 4.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0147109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024501 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.44795e+07s, dt:41696.2s, Cycle: 1143 +well_1Control: BHP (at the specified reference elevation): 48484238.23133892 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 6.53e-09 ) ; ( R ) = ( 3.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 2.32e-10 ) ; ( R ) = ( 8.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.90e-03 ) ; ( Rwell ) = ( 1.31e-10 ) ; ( R ) = ( 6.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 6.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.10e-03 ) ; ( Rwell ) = ( 1.01e-10 ) ; ( R ) = ( 7.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 5.42e-15 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0294202 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00490768 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.45212e+07s, dt:83392.3s, Cycle: 1144 +well_1Control: BHP (at the specified reference elevation): 48495707.31973098 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 9.27e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.50e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.72e-03 ) ; ( Rwell ) = ( 5.23e-10 ) ; ( R ) = ( 9.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.43e-03 ) ; ( Rwell ) = ( 4.00e-10 ) ; ( R ) = ( 8.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 2.26e-10 ) ; ( R ) = ( 7.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 5.70e-11 ) ; ( R ) = ( 6.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 8.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 3.22e-11 ) ; ( R ) = ( 4.80e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 9.11e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 5.63e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 8.54e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 9.98e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 5.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.01e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 9.35e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 7.51e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 8.77e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 9.40e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 7.04e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 8.22e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.81e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.36e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 6.60e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 7.71e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.26e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.09e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.62e-06 ) ; ( Rwell ) = ( 1.51e-14 ) ; ( R ) = ( 3.62e-06 ) ; + Last LinSolve(iter,res) = ( 8, 7.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0588168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00976401 +Time: 6.46046e+07s, dt:83392.3s, Cycle: 1145 +well_1Control: BHP (at the specified reference elevation): 48518589.88722712 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 6.95e-09 ) ; ( R ) = ( 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 9.23e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.33e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.22e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.40e-03 ) ; ( Rwell ) = ( 2.93e-10 ) ; ( R ) = ( 8.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 2.58e-10 ) ; ( R ) = ( 8.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.90e-03 ) ; ( Rwell ) = ( 2.27e-10 ) ; ( R ) = ( 7.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 2.00e-10 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.67e-05 ) ; ( Rwell ) = ( 7.81e-14 ) ; ( R ) = ( 7.67e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.06e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48541460.285299435 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0587722 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00969259 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.4688e+07s, dt:166785s, Cycle: 1146 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 6.94e-09 ) ; ( R ) = ( 1.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.97e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; ( R ) = ( 8.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 6.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; ( R ) = ( 6.72e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 9.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.36e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 5.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 9.91e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 2.89e-10 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 4.23e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 7.25e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.63e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.01e-05 ) ; ( Rwell ) = ( 9.46e-14 ) ; ( R ) = ( 9.01e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.117412 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0191602 +Time: 6.48548e+07s, dt:145228s, Cycle: 1147 +well_1Control: BHP (at the specified reference elevation): 48587078.94010666 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 6.91e-09 ) ; ( R ) = ( 1.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 7.57e-09 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.03e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 6.43e-09 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 6.23e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 6.05e-09 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 5.91e-09 ) ; ( R ) = ( 3.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 5.52e-09 ) ; ( R ) = ( 3.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 5.45e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 5.33e-09 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; ( R ) = ( 1.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.14e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.74e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 9.70e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 5.01e-09 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.102063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0168032 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.5e+07s, dt:72614.2s, Cycle: 1148 +well_1Control: BHP (at the specified reference elevation): 48626817.230403304 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 6.90e-09 ) ; ( R ) = ( 5.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 6.91e-10 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 3.86e-10 ) ; ( R ) = ( 9.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 2.22e-10 ) ; ( R ) = ( 6.28e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 1.33e-10 ) ; ( R ) = ( 4.97e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.17e-10 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.09e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 7.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 6.29e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.47e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 3.13e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.13e-04 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 5.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0509673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0084184 +compflowStatistics, reservoir: Pressure (min, average, max): 2.88178e+07, 2.88582e+07, 2.89692e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.63032e+07, 1.64546e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.625 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 24.8429, 715.783 } rm^3 +compflowStatistics, reservoir: Phase mass: { 16607.9, 699831 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2360.66, 217313 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 14247.2, 482518 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.7544, 11.0415 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 16588.1, 699820 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 16607.9, 0 }, { 2632.21, 697131 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.86076e+07, 2.87567e+07, 2.88364e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.6093e+07, 1.63219e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.264 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.264 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221028 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66308.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154720 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221028 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.28624e-07, 221028 } } kg +well_1Control: BHP (at the specified reference elevation): 48646701.5569935 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 136.939 +compflowStatistics: Max component CFL number: 188.129 +Time: 6.50726e+07s, dt:72614.2s, Cycle: 1149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 6.92e-10 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 3.92e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 2.20e-10 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 1.93e-10 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.50e-10 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.31e-10 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.55e-05 ) ; ( Rwell ) = ( 6.89e-16 ) ; ( R ) = ( 5.55e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.17e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48666580.67792594 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0509292 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00837966 +Time: 6.51452e+07s, dt:72614.2s, Cycle: 1150 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 6.90e-10 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.75e-10 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-05 ) ; ( Rwell ) = ( 1.40e-13 ) ; ( R ) = ( 4.17e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0508934 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00830359 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.52178e+07s, dt:145228s, Cycle: 1151 +well_1Control: BHP (at the specified reference elevation): 48686456.84503426 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 6.88e-09 ) ; ( R ) = ( 1.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 8.41e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 3.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 8.06e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 7.27e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 7.60e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 7.95e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 7.36e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 6.81e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 7.16e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 7.50e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 6.73e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.37e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 6.75e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 7.08e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 6.17e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.97e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 6.36e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 6.68e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 9.26e-10 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 5.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 5.59e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 5.99e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 6.30e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 8.14e-10 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 5.18e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.23e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 4.60e-10 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.21e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 4.65e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.92e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.04e-10 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 3.47e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.94e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 4.63e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.56e-10 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.20e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.69e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.11e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 4.35e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.12e-10 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 2.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.46e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 3.86e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.09e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.75e-10 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.73e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.24e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.63e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.85e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.41e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.53e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.04e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.41e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.62e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.11e-10 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.85e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.20e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.40e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.87e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 2.17e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.67e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.00e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 3.20e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.64e-10 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.01e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.50e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.82e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.00e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.44e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.34e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.65e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.82e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.27e-10 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.61e-05 ) ; ( Rwell ) = ( 1.68e-13 ) ; ( R ) = ( 4.61e-05 ) ; + Last LinSolve(iter,res) = ( 10, 8.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.101698 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0166216 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.53631e+07s, dt:72614.2s, Cycle: 1152 +well_1Control: BHP (at the specified reference elevation): 48726111.6438591 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 6.85e-09 ) ; ( R ) = ( 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 6.89e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 1.73e-10 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.36e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 7.65e-14 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0507878 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00823114 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.54357e+07s, dt:145228s, Cycle: 1153 +well_1Control: BHP (at the specified reference elevation): 48745968.414125934 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 6.85e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 6.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 5.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; ( R ) = ( 3.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 8.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 6.41e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 6.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 9.55e-10 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 8.41e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 7.39e-10 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 5.67e-10 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 4.99e-10 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 4.41e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 3.87e-10 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.41e-10 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.99e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.63e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 9.50e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.31e-10 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 9.51e-05 ) ; ( Rwell ) = ( 8.05e-14 ) ; ( R ) = ( 9.51e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.101489 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0164593 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.55809e+07s, dt:72614.2s, Cycle: 1154 +well_1Control: BHP (at the specified reference elevation): 48785596.99162241 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 6.83e-09 ) ; ( R ) = ( 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 6.84e-10 ) ; ( R ) = ( 9.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 1.73e-10 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.34e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 8.14e-14 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 48805431.08159583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0506849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00821352 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.56535e+07s, dt:145228s, Cycle: 1155 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 6.82e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 2.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.56e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 8.62e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.34e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 5.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 6.20e-10 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 5.46e-10 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 4.80e-10 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 9.70e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 4.21e-10 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 9.16e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 3.71e-10 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 8.64e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 3.26e-10 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 8.14e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.86e-10 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 7.68e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 7.24e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.41e-05 ) ; ( Rwell ) = ( 6.65e-14 ) ; ( R ) = ( 4.41e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.101284 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0163489 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.57988e+07s, dt:72614.2s, Cycle: 1156 +well_1Control: BHP (at the specified reference elevation): 48845009.004215814 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 6.80e-09 ) ; ( R ) = ( 5.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 6.81e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.66e-03 ) ; ( Rwell ) = ( 3.84e-10 ) ; ( R ) = ( 7.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.16e-10 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.87e-05 ) ; ( Rwell ) = ( 5.18e-14 ) ; ( R ) = ( 7.87e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0505838 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00808912 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.58714e+07s, dt:128629s, Cycle: 1157 +well_1Control: BHP (at the specified reference elevation): 48864814.1448041 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.28e-03 ) ; ( Rwell ) = ( 6.79e-09 ) ; ( R ) = ( 9.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 6.93e-09 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 6.05e-09 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 5.29e-09 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 5.25e-09 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.86e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.47e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; ( R ) = ( 8.47e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.83e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 5.07e-09 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 2.33e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 4.37e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.87e-05 ) ; ( Rwell ) = ( 1.10e-14 ) ; ( R ) = ( 5.87e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0895338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.014428 +Time: 6.6e+07s, dt:128629s, Cycle: 1158 +well_1Control: BHP (at the specified reference elevation): 48899846.767889455 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 6.78e-09 ) ; ( R ) = ( 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.46e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.45e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.42e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 9.19e-10 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.20e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.71e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 4.58e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.22e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 4.03e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 2.27e-10 ) ; ( R ) = ( 9.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-03 ) ; ( Rwell ) = ( 9.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.25e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.13e-03 ) ; ( Rwell ) = ( 2.00e-10 ) ; ( R ) = ( 8.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.07e-04 ) ; ( Rwell ) = ( 1.83e-13 ) ; ( R ) = ( 1.07e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.089431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0143796 +well_1Control: BHP (at the specified reference elevation): 48934848.60454363 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 2.90289e+07, 2.90693e+07, 2.91805e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.65032e+07, 1.66548e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.779 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 25.1578, 715.621 } rm^3 +compflowStatistics, reservoir: Phase mass: { 16885.3, 699788 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2397.01, 217394 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 14488.3, 482393 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.7787, 11.4825 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 16865.5, 699776 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 16885.3, 0 }, { 2666.99, 697052 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.88192e+07, 2.89679e+07, 2.90476e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.62935e+07, 1.65219e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.311 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.311 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221108 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66332.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154775 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221108 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 7.94416e-07, 221108 } } kg +compflowStatistics: Max phase CFL number: 241.571 +compflowStatistics: Max component CFL number: 331.857 +Time: 6.61286e+07s, dt:128629s, Cycle: 1159 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 6.76e-09 ) ; ( R ) = ( 9.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 8.36e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 7.48e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 7.34e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.55e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 7.21e-09 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 7.11e-09 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 7.01e-09 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.71e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 6.94e-09 ) ; ( R ) = ( 7.82e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.81e-04 ) ; ( Rwell ) = ( 7.31e-13 ) ; ( R ) = ( 1.81e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0893269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0144185 +Time: 6.62573e+07s, dt:128629s, Cycle: 1160 +well_1Control: BHP (at the specified reference elevation): 48969846.617038935 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 6.75e-09 ) ; ( R ) = ( 9.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.10e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 9.11e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 8.00e-10 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.49e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.90e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 7.04e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 6.19e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 5.44e-10 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.71e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.28e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.79e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.21e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.70e-10 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.26e-10 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 2.86e-10 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.63e-04 ) ; ( Rwell ) = ( 8.34e-15 ) ; ( R ) = ( 1.63e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0892247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.014504 +Time: 6.63859e+07s, dt:128629s, Cycle: 1161 +well_1Control: BHP (at the specified reference elevation): 49004792.41677491 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.36e-03 ) ; ( Rwell ) = ( 6.72e-09 ) ; ( R ) = ( 9.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 9.69e-09 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 9.03e-09 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 8.88e-09 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.79e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 8.74e-09 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 8.61e-09 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 8.47e-09 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 7.89e-09 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 5.29e-11 ) ; ( R ) = ( 9.78e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.11e-05 ) ; ( Rwell ) = ( 3.75e-14 ) ; ( R ) = ( 5.11e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0891189 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0143798 +Time: 6.65145e+07s, dt:128629s, Cycle: 1162 +well_1Control: BHP (at the specified reference elevation): 49039718.58838859 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 6.71e-09 ) ; ( R ) = ( 9.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.13e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.52e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.72e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 9.11e-10 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 8.01e-10 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.64e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 7.04e-10 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 6.19e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.79e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.44e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 5.44e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.84e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 4.79e-10 ) ; ( R ) = ( 6.95e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.50e-04 ) ; ( Rwell ) = ( 1.58e-13 ) ; ( R ) = ( 1.50e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0890137 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.014504 +Time: 6.66431e+07s, dt:128629s, Cycle: 1163 +well_1Control: BHP (at the specified reference elevation): 49074600.16561702 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 6.69e-09 ) ; ( R ) = ( 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.57e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 9.50e-09 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.22e-04 ) ; ( Rwell ) = ( 6.84e-13 ) ; ( R ) = ( 2.22e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0889057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0145067 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.67718e+07s, dt:228225s, Cycle: 1164 +well_1Control: BHP (at the specified reference elevation): 49109474.71908221 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 6.68e-09 ) ; ( R ) = ( 1.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 1.47e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.34e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 9.78e-09 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 9.16e-09 ) ; ( R ) = ( 1.47e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 8.58e-09 ) ; ( R ) = ( 5.33e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.22e-02 ) ; ( Rwell ) = ( 6.75e-09 ) ; ( R ) = ( 8.22e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.53e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 9.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 5.39e-09 ) ; ( R ) = ( 6.39e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 9.13e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 5.27e-09 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 8.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 5.16e-09 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 4.85e-13 ) ; ( R ) = ( 6.37e-04 ) ; + Last LinSolve(iter,res) = ( 10, 9.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.157494 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0254186 +Time: 6.7e+07s, dt:228225s, Cycle: 1165 +well_1Control: BHP (at the specified reference elevation): 49171173.497662686 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 6.64e-09 ) ; ( R ) = ( 1.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 4.93e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.10e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 9.10e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 3.81e-09 ) ; ( R ) = ( 6.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 3.36e-09 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 1.03e-13 ) ; ( R ) = ( 9.03e-04 ) ; + Last LinSolve(iter,res) = ( 11, 6.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.157131 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0250845 +compflowStatistics, reservoir: Pressure (min, average, max): 2.92481e+07, 2.92885e+07, 2.93998e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.67026e+07, 1.68543e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 740.938 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 25.484, 715.454 } rm^3 +compflowStatistics, reservoir: Phase mass: { 17173.6, 699743 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2435.07, 217479 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 14738.5, 482264 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.2551, 11.6313 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 17153.3, 699731 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 17173.6, 0 }, { 2703.84, 696969 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.9039e+07, 2.91873e+07, 2.92667e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.64935e+07, 1.67213e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.359 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.359 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221190 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66357.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154833 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221190 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 3.25522e-06, 221190 } } kg +well_1Control: BHP (at the specified reference elevation): 49232820.980549246 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 426.805 +compflowStatistics: Max component CFL number: 586.294 +Time: 6.72282e+07s, dt:228225s, Cycle: 1166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 6.61e-09 ) ; ( R ) = ( 1.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 5.12e-08 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 6.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.84e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 9.27e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.72e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.47e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 4.29e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 9.50e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 8.33e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 1.49e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.15e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.58e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; ( R ) = ( 9.58e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 8.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 7.63e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 1.28e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.86e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 3.34e-09 ) ; ( R ) = ( 8.88e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 7.42e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 6.92e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.11e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.62e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.91e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 7.91e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 6.55e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 6.27e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 9.54e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 1.40e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.13e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; ( R ) = ( 8.13e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 5.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 5.67e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 8.21e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 1.21e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 5.09e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 5.16e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 7.04e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 1.05e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 7.31e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 4.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.66e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 6.03e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 9.03e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 1.65e-13 ) ; ( R ) = ( 4.67e-04 ) ; + Last LinSolve(iter,res) = ( 10, 8.63e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49294417.95070502 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.156782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0249211 +Time: 6.74565e+07s, dt:228225s, Cycle: 1167 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 6.59e-09 ) ; ( R ) = ( 1.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 3.58e-09 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 7.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.06e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 7.06e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 9.27e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 9.91e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 6.03e-14 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 11, 6.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.156455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0247331 +Time: 6.76847e+07s, dt:228225s, Cycle: 1168 +well_1Control: BHP (at the specified reference elevation): 49355985.825690046 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 6.57e-09 ) ; ( R ) = ( 1.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 4.16e-08 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 4.03e-08 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 5.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 9.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 3.29e-09 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 9.70e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 2.90e-09 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 9.51e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 9.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 8.99e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.67e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 7.67e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 8.71e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 8.42e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.39e-10 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.38e-05 ) ; ( Rwell ) = ( 1.76e-13 ) ; ( R ) = ( 7.38e-05 ) ; + Last LinSolve(iter,res) = ( 10, 9.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.156145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0246935 +Time: 6.79129e+07s, dt:87099.8s, Cycle: 1169 +well_1Control: BHP (at the specified reference elevation): 49417491.43769753 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 6.54e-09 ) ; ( R ) = ( 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; ( R ) = ( 9.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; ( R ) = ( 6.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 5.62e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-05 ) ; ( Rwell ) = ( 2.71e-14 ) ; ( R ) = ( 1.40e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.89e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49441021.885000855 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0594921 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00937719 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.8e+07s, dt:174200s, Cycle: 1170 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 6.55e-09 ) ; ( R ) = ( 1.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.37e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; ( R ) = ( 8.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 3.70e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.00e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 3.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 9.54e-10 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.38e-10 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 4.72e-10 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.37e-04 ) ; ( Rwell ) = ( 2.36e-13 ) ; ( R ) = ( 1.37e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.118899 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0187847 +compflowStatistics, reservoir: Pressure (min, average, max): 2.94364e+07, 2.94768e+07, 2.95882e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.69017e+07, 1.70535e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.075 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 25.7643, 715.311 } rm^3 +compflowStatistics, reservoir: Phase mass: { 17421.9, 699704 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2467.75, 217552 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 14954.2, 482152 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.9841, 11.7762 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 17401.9, 699692 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 17421.9, 0 }, { 2735.18, 696898 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.92276e+07, 2.93756e+07, 2.9455e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.66929e+07, 1.69204e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.401 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.401 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221261 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66378.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154883 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221261 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 1.0743e-05, 221261 } } kg +well_1Control: BHP (at the specified reference elevation): 49487939.481069714 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 324.608 +compflowStatistics: Max component CFL number: 445.889 +Time: 6.81742e+07s, dt:174200s, Cycle: 1171 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 6.51e-09 ) ; ( R ) = ( 1.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 6.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 6.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 7.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 8.19e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 8.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 6.22e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 9.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 9.97e-10 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 8.79e-10 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 7.71e-10 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.03e-04 ) ; ( Rwell ) = ( 2.89e-13 ) ; ( R ) = ( 3.03e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.11874 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0188401 +Time: 6.83484e+07s, dt:174200s, Cycle: 1172 +well_1Control: BHP (at the specified reference elevation): 49534816.783116035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 6.49e-09 ) ; ( R ) = ( 1.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 9.26e-09 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 9.02e-09 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 8.79e-09 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 8.62e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 8.43e-09 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 8.32e-09 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 7.86e-09 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 6.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 7.73e-09 ) ; ( R ) = ( 3.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 7.67e-09 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 7.62e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 7.63e-09 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 7.59e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 7.55e-09 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 8.77e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 7.51e-09 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 3.69e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 7.49e-09 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.09e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 7.47e-09 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.07e-04 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 1.07e-04 ) ; + Last LinSolve(iter,res) = ( 10, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.118575 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0188102 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.85226e+07s, dt:87099.8s, Cycle: 1173 +well_1Control: BHP (at the specified reference elevation): 49581634.850981906 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 6.47e-09 ) ; ( R ) = ( 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 9.08e-10 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 5.14e-10 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 4.52e-10 ) ; ( R ) = ( 9.02e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.68e-03 ) ; ( Rwell ) = ( 3.97e-10 ) ; ( R ) = ( 9.68e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.20e-03 ) ; ( Rwell ) = ( 3.49e-10 ) ; ( R ) = ( 9.20e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.75e-03 ) ; ( Rwell ) = ( 3.07e-10 ) ; ( R ) = ( 8.75e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 2.70e-10 ) ; ( R ) = ( 7.52e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 2.38e-10 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.40e-03 ) ; ( Rwell ) = ( 2.09e-10 ) ; ( R ) = ( 8.40e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.03e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 6.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 4.62e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.85e-05 ) ; ( Rwell ) = ( 3.52e-14 ) ; ( R ) = ( 2.85e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0592129 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00943509 +Time: 6.86097e+07s, dt:87099.8s, Cycle: 1174 +well_1Control: BHP (at the specified reference elevation): 49605060.42266275 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 6.46e-09 ) ; ( R ) = ( 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 9.10e-10 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 5.13e-10 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.93e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 3.93e-10 ) ; ( R ) = ( 9.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 3.46e-10 ) ; ( R ) = ( 8.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 7.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 9.68e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 9.95e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.44e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.07e-05 ) ; ( Rwell ) = ( 3.90e-15 ) ; ( R ) = ( 2.07e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0591726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00939918 +Time: 6.86968e+07s, dt:87099.8s, Cycle: 1175 +well_1Control: BHP (at the specified reference elevation): 49628473.69711256 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 9.61e-09 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 6.33e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.98e-03 ) ; ( Rwell ) = ( 9.55e-09 ) ; ( R ) = ( 6.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 9.51e-09 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.02e-03 ) ; ( Rwell ) = ( 9.48e-09 ) ; ( R ) = ( 8.02e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 7.63e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 3.39e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 5.62e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 6.65e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 7.15e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.77e-03 ) ; ( Rwell ) = ( 1.50e-10 ) ; ( R ) = ( 6.77e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 3.20e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 5.27e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 6.23e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 6.70e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 3.02e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 4.94e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 5.84e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 6.27e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.06e-03 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 6.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 2.85e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 4.63e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 5.47e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 5.88e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 2.68e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 4.34e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 5.13e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 5.51e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 8.95e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 2.53e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 4.07e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 4.80e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 5.16e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 7.87e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 2.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 3.82e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 4.50e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 4.83e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 6.92e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.24e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 3.58e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 4.22e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 4.53e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 6.08e-11 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.11e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 3.36e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 3.95e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 4.24e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 5.35e-11 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.26e-05 ) ; ( Rwell ) = ( 3.76e-14 ) ; ( R ) = ( 2.26e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0591338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00944886 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.87839e+07s, dt:43549.9s, Cycle: 1176 +well_1Control: BHP (at the specified reference elevation): 49651872.55995788 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 3.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 2.27e-10 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.77e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 5.07e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-04 ) ; ( Rwell ) = ( 4.35e-16 ) ; ( R ) = ( 1.80e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295493 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00473677 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.88274e+07s, dt:87099.8s, Cycle: 1177 +well_1Control: BHP (at the specified reference elevation): 49663575.23463644 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 6.43e-09 ) ; ( R ) = ( 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 9.04e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 5.10e-10 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.16e-03 ) ; ( Rwell ) = ( 2.87e-10 ) ; ( R ) = ( 8.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 2.53e-10 ) ; ( R ) = ( 7.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.26e-03 ) ; ( Rwell ) = ( 2.22e-10 ) ; ( R ) = ( 7.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 6.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 5.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 8.53e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.68e-05 ) ; ( Rwell ) = ( 4.18e-15 ) ; ( R ) = ( 4.68e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0590765 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00945473 +Time: 6.89145e+07s, dt:85451.7s, Cycle: 1178 +well_1Control: BHP (at the specified reference elevation): 49686957.352075994 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; ( R ) = ( 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.38e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 9.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.43e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; ( R ) = ( 7.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.03e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; ( R ) = ( 8.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.63e-05 ) ; ( Rwell ) = ( 8.94e-13 ) ; ( R ) = ( 3.63e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.14e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49709889.677445784 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0579204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00923938 +Time: 6.9e+07s, dt:85451.7s, Cycle: 1179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 6.42e-09 ) ; ( R ) = ( 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 8.59e-10 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 6.60e-10 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 1.68e-10 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.29e-10 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 1.12e-10 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.11e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 6.39e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.90e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.92e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.91e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.41e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.67e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.55e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.48e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 6.94e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.44e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.20e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 6.07e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 6.51e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.23e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.88e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.69e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 6.10e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 9.60e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.03e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.57e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.34e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 5.72e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 8.44e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.29e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.00e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 5.36e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.66e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.02e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.69e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.03e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.50e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.77e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.40e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.71e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.74e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.53e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.12e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.42e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.20e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.31e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.87e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.14e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 5.53e-06 ) ; ( Rwell ) = ( 1.22e-14 ) ; ( R ) = ( 5.53e-06 ) ; + Last LinSolve(iter,res) = ( 8, 6.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0578837 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00921159 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +compflowStatistics, reservoir: Pressure (min, average, max): 2.96176e+07, 2.96581e+07, 2.97696e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.71007e+07, 1.72526e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.207 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 26.0347, 715.172 } rm^3 +compflowStatistics, reservoir: Phase mass: { 17661.9, 699666 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2498.57, 217622 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 15163.3, 482044 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.0828, 12.4029 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 17641.8, 699654 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 17661.9, 0 }, { 2764.63, 696830 } } kg +well_1Control: BHP (at the specified reference elevation): 49732799.525017485 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.94091e+07, 2.9557e+07, 2.96363e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.68921e+07, 1.71193e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.441 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.441 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221330 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66398.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154931 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221330 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.98785e-05, 221330 } } kg +compflowStatistics: Max phase CFL number: 158.693 +compflowStatistics: Max component CFL number: 217.975 +Time: 6.90855e+07s, dt:42725.9s, Cycle: 1180 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 2.17e-10 ) ; ( R ) = ( 9.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 1.22e-10 ) ; ( R ) = ( 7.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 1.07e-10 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 9.50e-11 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 8.29e-11 ) ; ( R ) = ( 6.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 7.28e-11 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 6.40e-11 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 5.62e-11 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 4.96e-11 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 4.36e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 3.82e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.09e-05 ) ; ( Rwell ) = ( 1.65e-14 ) ; ( R ) = ( 4.09e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0289239 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00461369 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.91282e+07s, dt:21362.9s, Cycle: 1181 +well_1Control: BHP (at the specified reference elevation): 49744261.40182127 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 5.51e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 9.95e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.97e-05 ) ; ( Rwell ) = ( 3.12e-15 ) ; ( R ) = ( 4.97e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.90e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49749995.046170786 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0144573 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231349 +Time: 6.91495e+07s, dt:21362.9s, Cycle: 1182 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 5.50e-11 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 9.20e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.02e-06 ) ; ( Rwell ) = ( 4.10e-15 ) ; ( R ) = ( 9.02e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231835 +Time: 6.91709e+07s, dt:21362.9s, Cycle: 1183 +well_1Control: BHP (at the specified reference elevation): 49755729.09444043 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.44e-11 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 8.53e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 9.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144506 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00232207 +Time: 6.91923e+07s, dt:21362.9s, Cycle: 1184 +well_1Control: BHP (at the specified reference elevation): 49761458.50102915 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.39e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 5.48e-11 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 4.19e-11 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.25e-11 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.76e-05 ) ; ( Rwell ) = ( 2.42e-15 ) ; ( R ) = ( 3.76e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144505 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00232385 +Time: 6.92136e+07s, dt:21362.9s, Cycle: 1185 +well_1Control: BHP (at the specified reference elevation): 49767190.55123145 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 5.46e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.40e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0023252 +Time: 6.9235e+07s, dt:21362.9s, Cycle: 1186 +well_1Control: BHP (at the specified reference elevation): 49772915.9812403 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 9.39e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.31e-05 ) ; ( Rwell ) = ( 6.56e-16 ) ; ( R ) = ( 5.31e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144465 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00232373 +Time: 6.92564e+07s, dt:21362.9s, Cycle: 1187 +well_1Control: BHP (at the specified reference elevation): 49778646.57590438 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 5.48e-11 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.11e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.09e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.42e-05 ) ; ( Rwell ) = ( 1.92e-16 ) ; ( R ) = ( 5.42e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144424 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00232162 +Time: 6.92777e+07s, dt:21362.9s, Cycle: 1188 +well_1Control: BHP (at the specified reference elevation): 49784378.254343815 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 5.43e-11 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.40e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.77e-05 ) ; ( Rwell ) = ( 7.54e-16 ) ; ( R ) = ( 3.77e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231749 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.92991e+07s, dt:10681.5s, Cycle: 1189 +well_1Control: BHP (at the specified reference elevation): 49790105.54147274 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 7.57e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 9.56e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 8.44e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 7.46e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.27e-05 ) ; ( Rwell ) = ( 4.70e-16 ) ; ( R ) = ( 2.27e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721931 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115792 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.93098e+07s, dt:5340.73s, Cycle: 1190 +well_1Control: BHP (at the specified reference elevation): 49792968.99930857 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.79e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 3.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 6.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000578752 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.93151e+07s, dt:10681.5s, Cycle: 1191 +well_1Control: BHP (at the specified reference elevation): 49794394.36762637 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 1.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 9.57e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.67e-06 ) ; ( Rwell ) = ( 2.97e-15 ) ; ( R ) = ( 3.67e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0072207 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115585 +Time: 6.93258e+07s, dt:10681.5s, Cycle: 1192 +well_1Control: BHP (at the specified reference elevation): 49797260.1148068 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 7.56e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 9.48e-12 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 8.37e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 7.39e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.54e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.55e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.31e-05 ) ; ( Rwell ) = ( 3.72e-16 ) ; ( R ) = ( 2.31e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721791 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115355 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.93365e+07s, dt:5340.73s, Cycle: 1193 +well_1Control: BHP (at the specified reference elevation): 49800123.322022736 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 3.78e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 7.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360927 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000576533 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.93418e+07s, dt:10681.5s, Cycle: 1194 +well_1Control: BHP (at the specified reference elevation): 49801550.56713873 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 1.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 4.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 9.56e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 8.43e-12 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.13e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.66e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.38e-05 ) ; ( Rwell ) = ( 2.35e-15 ) ; ( R ) = ( 3.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721882 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115134 +Time: 6.93525e+07s, dt:10681.5s, Cycle: 1195 +well_1Control: BHP (at the specified reference elevation): 49804414.34373096 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 7.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 9.86e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 7.74e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.72e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.69e-05 ) ; ( Rwell ) = ( 1.48e-15 ) ; ( R ) = ( 1.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49807277.15573342 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00721645 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115094 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.93632e+07s, dt:5340.73s, Cycle: 1196 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 3.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 9.13e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360851 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000575196 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.93685e+07s, dt:10681.5s, Cycle: 1197 +well_1Control: BHP (at the specified reference elevation): 49808704.985551536 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 1.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 8.31e-12 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 4.62e-15 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721808 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114989 +Time: 6.93792e+07s, dt:10681.5s, Cycle: 1198 +well_1Control: BHP (at the specified reference elevation): 49811567.68463191 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 7.52e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 8.13e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.16e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 9.40e-16 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721512 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0011492 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.93899e+07s, dt:5340.73s, Cycle: 1199 +well_1Control: BHP (at the specified reference elevation): 49814430.281551 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 3.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 9.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00361075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000574488 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.93952e+07s, dt:10681.5s, Cycle: 1200 +well_1Control: BHP (at the specified reference elevation): 49815859.36492992 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 4.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 7.99e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.50e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.36e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.02e-05 ) ; ( Rwell ) = ( 5.08e-15 ) ; ( R ) = ( 4.02e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721816 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0011479 +Time: 6.94059e+07s, dt:10681.5s, Cycle: 1201 +well_1Control: BHP (at the specified reference elevation): 49818719.589742035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 7.50e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 9.27e-12 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 6.35e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.00e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.84e-05 ) ; ( Rwell ) = ( 1.53e-15 ) ; ( R ) = ( 2.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721399 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114678 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.94166e+07s, dt:5340.73s, Cycle: 1202 +well_1Control: BHP (at the specified reference elevation): 49821581.473847896 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 3.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360847 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000573005 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.94219e+07s, dt:10681.5s, Cycle: 1203 +well_1Control: BHP (at the specified reference elevation): 49823011.88364105 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 2.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 7.23e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.12e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.53e-05 ) ; ( Rwell ) = ( 6.74e-15 ) ; ( R ) = ( 2.53e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721637 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114479 +Time: 6.94326e+07s, dt:10681.5s, Cycle: 1204 +well_1Control: BHP (at the specified reference elevation): 49825870.89678939 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 7.49e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 8.86e-12 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 7.65e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.83e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.75e-05 ) ; ( Rwell ) = ( 6.37e-16 ) ; ( R ) = ( 2.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721252 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114642 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.94433e+07s, dt:5340.73s, Cycle: 1205 +well_1Control: BHP (at the specified reference elevation): 49828731.90408905 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.74e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 3.74e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 7.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00057368 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.94486e+07s, dt:10681.5s, Cycle: 1206 +well_1Control: BHP (at the specified reference elevation): 49830160.54901986 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 1.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.20e-05 ) ; ( Rwell ) = ( 1.99e-15 ) ; ( R ) = ( 2.20e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.65e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49833019.527151585 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00721509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114893 +Time: 6.94593e+07s, dt:10681.5s, Cycle: 1207 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 7.47e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 9.37e-12 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 8.27e-12 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.67e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 1.17e-15 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115045 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.947e+07s, dt:5340.73s, Cycle: 1208 +well_1Control: BHP (at the specified reference elevation): 49835879.99511778 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.74e-04 ) ; ( Rwell ) = ( 6.37e-09 ) ; ( R ) = ( 3.74e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 8.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360559 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000575515 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.94753e+07s, dt:10681.5s, Cycle: 1209 +well_1Control: BHP (at the specified reference elevation): 49837307.61307119 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 1.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.93e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 3.72e-16 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49840166.43047005 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00721446 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115236 +Time: 6.9486e+07s, dt:10681.5s, Cycle: 1210 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 7.49e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 5.58e-12 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.65e-05 ) ; ( Rwell ) = ( 2.11e-15 ) ; ( R ) = ( 2.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00720996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0011535 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.94967e+07s, dt:5340.73s, Cycle: 1211 +well_1Control: BHP (at the specified reference elevation): 49843026.45767006 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 3.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 7.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49844455.265506074 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00360485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000577067 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.9502e+07s, dt:10681.5s, Cycle: 1212 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 1.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.23e-05 ) ; ( Rwell ) = ( 2.52e-15 ) ; ( R ) = ( 2.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721113 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115477 +Time: 6.95127e+07s, dt:10681.5s, Cycle: 1213 +well_1Control: BHP (at the specified reference elevation): 49847313.52742924 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 7.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 5.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 8.22e-12 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 7.19e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.95e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.86e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.65e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.47e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.47e-05 ) ; ( Rwell ) = ( 2.62e-16 ) ; ( R ) = ( 2.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00720827 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115541 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.95234e+07s, dt:5340.73s, Cycle: 1214 +well_1Control: BHP (at the specified reference elevation): 49850173.04252807 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.76e-04 ) ; ( Rwell ) = ( 6.36e-09 ) ; ( R ) = ( 3.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 9.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000577938 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.95287e+07s, dt:10681.5s, Cycle: 1215 +well_1Control: BHP (at the specified reference elevation): 49851599.80057792 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.22e-05 ) ; ( Rwell ) = ( 2.17e-15 ) ; ( R ) = ( 2.22e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00721138 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115605 +Time: 6.95394e+07s, dt:10681.5s, Cycle: 1216 +well_1Control: BHP (at the specified reference elevation): 49854456.60762483 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 7.53e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 4.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 9.46e-12 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 8.35e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 7.41e-12 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.68e-05 ) ; ( Rwell ) = ( 1.97e-15 ) ; ( R ) = ( 2.68e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0072072 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115629 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.95501e+07s, dt:5340.73s, Cycle: 1217 +well_1Control: BHP (at the specified reference elevation): 49857314.390786126 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 3.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 7.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360334 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000578156 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.95554e+07s, dt:10681.5s, Cycle: 1218 +well_1Control: BHP (at the specified reference elevation): 49858742.69232249 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 5.98e-12 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.65e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.83e-05 ) ; ( Rwell ) = ( 2.84e-15 ) ; ( R ) = ( 2.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00720854 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115629 +Time: 6.95661e+07s, dt:10681.5s, Cycle: 1219 +well_1Control: BHP (at the specified reference elevation): 49861598.45945141 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 7.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 5.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 4.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 9.32e-12 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 8.21e-12 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.22e-06 ) ; ( Rwell ) = ( 1.30e-15 ) ; ( R ) = ( 9.22e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00720537 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115608 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.95768e+07s, dt:5340.73s, Cycle: 1220 +well_1Control: BHP (at the specified reference elevation): 49864456.095820636 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-04 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 3.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 9.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360275 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000578151 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.95821e+07s, dt:10681.5s, Cycle: 1221 +well_1Control: BHP (at the specified reference elevation): 49865883.3814708 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 1.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.70e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.51e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.20e-05 ) ; ( Rwell ) = ( 2.71e-15 ) ; ( R ) = ( 2.20e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00720772 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115548 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.95928e+07s, dt:21362.9s, Cycle: 1222 +well_1Control: BHP (at the specified reference elevation): 49868738.88746861 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 5.44e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.72e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 8.71e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.37e-05 ) ; ( Rwell ) = ( 3.80e-15 ) ; ( R ) = ( 5.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49874452.135087036 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.014407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00230842 +Time: 6.96142e+07s, dt:21362.9s, Cycle: 1223 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 5.37e-11 ) ; ( R ) = ( 5.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.40e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-04 ) ; ( Rwell ) = ( 9.14e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 5.06e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144032 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00230435 +Time: 6.96355e+07s, dt:21362.9s, Cycle: 1224 +well_1Control: BHP (at the specified reference elevation): 49880163.78304735 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.46e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 8.32e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229965 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.96569e+07s, dt:42725.9s, Cycle: 1225 +well_1Control: BHP (at the specified reference elevation): 49885872.64877963 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.14e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 7.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 1.07e-10 ) ; ( R ) = ( 6.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 9.39e-11 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.31e-03 ) ; ( Rwell ) = ( 8.22e-11 ) ; ( R ) = ( 8.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 7.22e-11 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 6.38e-11 ) ; ( R ) = ( 6.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 5.62e-11 ) ; ( R ) = ( 6.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 4.95e-11 ) ; ( R ) = ( 5.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 4.34e-11 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.15e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 8.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 7.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 7.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.31e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.07e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 7.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 7.62e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.45e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 5.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 6.67e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 8.93e-12 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 6.25e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 9.41e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 4.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 5.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 8.82e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 21362.93027791381 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 5.39e-11 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 5.54e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 4.14e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.65e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.21e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.38e-05 ) ; ( Rwell ) = ( 1.02e-15 ) ; ( R ) = ( 5.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49891584.22631726 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143995 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0022931 +coupledFlowAndWells: sub-step = 0, accepted dt = 21362.93027791381, remaining dt = 21362.93027791381 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.42e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.41e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.06e-05 ) ; ( Rwell ) = ( 6.66e-15 ) ; ( R ) = ( 2.06e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143964 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229129 +Time: 6.96996e+07s, dt:21362.9s, Cycle: 1226 +well_1Control: BHP (at the specified reference elevation): 49897295.17630963 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 5.44e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.69e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.34e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 8.38e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.24e-05 ) ; ( Rwell ) = ( 3.10e-15 ) ; ( R ) = ( 3.24e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014394 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229755 +Time: 6.9721e+07s, dt:21362.9s, Cycle: 1227 +well_1Control: BHP (at the specified reference elevation): 49903006.214102104 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 1.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 2.85e-10 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.62e-10 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.59e-10 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.56e-10 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.54e-10 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.52e-10 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.50e-10 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.48e-10 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.47e-10 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.46e-10 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.45e-10 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.44e-10 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.02e-05 ) ; ( Rwell ) = ( 1.99e-13 ) ; ( R ) = ( 4.02e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143917 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00230256 +Time: 6.97424e+07s, dt:21362.9s, Cycle: 1228 +well_1Control: BHP (at the specified reference elevation): 49908716.247322954 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 5.35e-11 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.02e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.66e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.34e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 9.59e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.05e-05 ) ; ( Rwell ) = ( 2.69e-15 ) ; ( R ) = ( 3.05e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143893 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00230671 +Time: 6.97637e+07s, dt:21362.9s, Cycle: 1229 +well_1Control: BHP (at the specified reference elevation): 49914425.14216985 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.33e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 5.33e-11 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.01e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.65e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 9.43e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 7.75e-12 ) ; ( R ) = ( 7.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143838 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231086 +Time: 6.97851e+07s, dt:21362.9s, Cycle: 1230 +well_1Control: BHP (at the specified reference elevation): 49920129.65432047 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.32e-09 ) ; ( R ) = ( 1.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.40e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 7.35e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.64e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 6.89e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 6.46e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.70e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.06e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.09e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.58e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.30e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 7.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.28e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.22e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-05 ) ; ( Rwell ) = ( 5.79e-17 ) ; ( R ) = ( 1.58e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143862 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231258 +Time: 6.98065e+07s, dt:21362.9s, Cycle: 1231 +well_1Control: BHP (at the specified reference elevation): 49925832.27280091 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 5.34e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.03e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.58e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49931530.77915301 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231306 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.98278e+07s, dt:42725.9s, Cycle: 1232 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; ( R ) = ( 3.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.71e-03 ) ; ( Rwell ) = ( 2.13e-10 ) ; ( R ) = ( 8.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.56e-03 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 7.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.30e-03 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 7.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 9.33e-11 ) ; ( R ) = ( 6.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.67e-03 ) ; ( Rwell ) = ( 8.18e-11 ) ; ( R ) = ( 6.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.07e-03 ) ; ( Rwell ) = ( 7.18e-11 ) ; ( R ) = ( 6.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 6.35e-11 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 5.54e-11 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.27e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 4.87e-11 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 4.28e-11 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.41e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.77e-11 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 6.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 7.47e-12 ) ; ( R ) = ( 5.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.30e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49942935.5734853 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0287555 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00461949 +Time: 6.98705e+07s, dt:42725.9s, Cycle: 1233 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; ( R ) = ( 3.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 2.12e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.83e-03 ) ; ( Rwell ) = ( 1.63e-10 ) ; ( R ) = ( 9.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.00e-03 ) ; ( Rwell ) = ( 1.25e-10 ) ; ( R ) = ( 9.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.47e-03 ) ; ( Rwell ) = ( 1.10e-10 ) ; ( R ) = ( 8.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 9.67e-11 ) ; ( R ) = ( 8.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.51e-03 ) ; ( Rwell ) = ( 8.48e-11 ) ; ( R ) = ( 7.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 7.46e-11 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 6.57e-11 ) ; ( R ) = ( 6.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 5.77e-11 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 5.08e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 4.46e-11 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 3.91e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 3.48e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.77e-05 ) ; ( Rwell ) = ( 1.69e-14 ) ; ( R ) = ( 5.77e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0287461 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00460464 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 6.99133e+07s, dt:21362.9s, Cycle: 1234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 49954343.06664023 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 6.31e-09 ) ; ( R ) = ( 1.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 5.38e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 2.00e-12 ) ; ( R ) = ( 9.13e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49960046.97622703 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143659 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229948 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.99346e+07s, dt:42725.9s, Cycle: 1235 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; ( R ) = ( 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.13e-10 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.04e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.63e-10 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.43e-10 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.26e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.11e-10 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.86e-03 ) ; ( Rwell ) = ( 9.76e-11 ) ; ( R ) = ( 8.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.21e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 7.84e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 9.15e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 9.80e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 4.89e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.35e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 8.58e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 9.19e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.58e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 1.18e-12 ) ; ( R ) = ( 7.55e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0287304 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0046001 +Time: 6.99774e+07s, dt:22645.9s, Cycle: 1236 +well_1Control: BHP (at the specified reference elevation): 49971451.45601548 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; ( R ) = ( 1.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.24e-05 ) ; ( Rwell ) = ( 3.31e-13 ) ; ( R ) = ( 5.24e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0152224 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244298 +Time: 7e+07s, dt:22645.9s, Cycle: 1237 +well_1Control: BHP (at the specified reference elevation): 49977496.76697542 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; ( R ) = ( 1.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 5.92e-11 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.59e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.28e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.87e-05 ) ; ( Rwell ) = ( 6.90e-15 ) ; ( R ) = ( 4.87e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49983542.42136724 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0152197 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244638 +compflowStatistics, reservoir: Pressure (min, average, max): 2.98038e+07, 2.98443e+07, 2.99559e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.72994e+07, 1.74514e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.342 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 26.3128, 715.03 } rm^3 +compflowStatistics, reservoir: Phase mass: { 17909.2, 699627 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2530.44, 217693 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 15378.8, 481933 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.224, 12.6123 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 17889, 699614 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 17909.2, 0 }, { 2794.44, 696759 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.95956e+07, 2.97433e+07, 2.98225e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.70911e+07, 1.7318e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.483 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.483 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221400 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66420 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 154980 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221400 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 8.55746e-05, 221400 } } kg +compflowStatistics: Max phase CFL number: 41.9116 +compflowStatistics: Max component CFL number: 57.5661 +Time: 7.00226e+07s, dt:22645.9s, Cycle: 1238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.30e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 5.96e-11 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.38e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.75e-05 ) ; ( Rwell ) = ( 3.68e-15 ) ; ( R ) = ( 4.75e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.86e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 49989585.26942871 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0152172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244837 +Time: 7.00453e+07s, dt:22645.9s, Cycle: 1239 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.29e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 6.00e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.40e-11 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.64e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.33e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.03e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 7.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 7.01e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 6.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 9.87e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 6.16e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 9.25e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.77e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 5.39e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 8.09e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 9.44e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 5.06e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 7.59e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 8.85e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 9.49e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 1.41e-12 ) ; ( R ) = ( 7.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0152122 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244856 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.00679e+07s, dt:11323s, Cycle: 1240 +well_1Control: BHP (at the specified reference elevation): 49995623.61491402 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 8.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 8.60e-12 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.99e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.60e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 9.83e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 1.26e-15 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00760621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122428 +Time: 7.00793e+07s, dt:11323s, Cycle: 1241 +well_1Control: BHP (at the specified reference elevation): 49998643.47129583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 8.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.11e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 7.15e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.76e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 1.45e-15 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.007605 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122516 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.00906e+07s, dt:5661.48s, Cycle: 1242 +well_1Control: BHP (at the specified reference elevation): 50001663.69928616 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 4.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 3.36e-12 ) ; ( R ) = ( 9.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00380409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000612646 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.00962e+07s, dt:11323s, Cycle: 1243 +well_1Control: BHP (at the specified reference elevation): 50003171.420540735 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; ( R ) = ( 1.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.43e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.28e-05 ) ; ( Rwell ) = ( 3.83e-15 ) ; ( R ) = ( 2.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.67e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50006190.44370976 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00760765 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122608 +Time: 7.01076e+07s, dt:11323s, Cycle: 1244 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 8.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 8.02e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 2.94e-15 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00760331 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122645 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.01189e+07s, dt:5661.48s, Cycle: 1245 +well_1Control: BHP (at the specified reference elevation): 50009211.138664335 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 4.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-04 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 8.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00380158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000613384 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.01246e+07s, dt:11323s, Cycle: 1246 +well_1Control: BHP (at the specified reference elevation): 50010719.416495256 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; ( R ) = ( 1.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-05 ) ; ( Rwell ) = ( 2.77e-15 ) ; ( R ) = ( 1.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00760397 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122662 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.01359e+07s, dt:22645.9s, Cycle: 1247 +well_1Control: BHP (at the specified reference elevation): 50013739.79980537 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 6.04e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 8.98e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.95e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.62e-05 ) ; ( Rwell ) = ( 5.30e-15 ) ; ( R ) = ( 3.62e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0152019 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024518 +Time: 7.01585e+07s, dt:22645.9s, Cycle: 1248 +well_1Control: BHP (at the specified reference elevation): 50019781.49629815 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.87e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 8.62e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 7.60e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 9.64e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.91e-05 ) ; ( Rwell ) = ( 1.10e-15 ) ; ( R ) = ( 2.91e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244852 +Time: 7.01812e+07s, dt:22645.9s, Cycle: 1249 +well_1Control: BHP (at the specified reference elevation): 50025823.69405007 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 5.99e-11 ) ; ( R ) = ( 5.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 8.49e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.46e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 6.99e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 6.13e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151929 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244771 +Time: 7.02038e+07s, dt:22645.9s, Cycle: 1250 +well_1Control: BHP (at the specified reference elevation): 50031863.200903326 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 6.05e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.43e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.02e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.66e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.35e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.37e-05 ) ; ( Rwell ) = ( 1.35e-14 ) ; ( R ) = ( 7.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151935 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244598 +Time: 7.02265e+07s, dt:22645.9s, Cycle: 1251 +well_1Control: BHP (at the specified reference elevation): 50037906.07880688 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 8.69e-10 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 8.46e-10 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.43e-10 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 8.40e-10 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 8.39e-10 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 8.36e-10 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 8.34e-10 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 8.32e-10 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.30e-10 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.29e-10 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.28e-10 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 8.27e-10 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.44e-05 ) ; ( Rwell ) = ( 1.41e-13 ) ; ( R ) = ( 3.44e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.01519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024434 +Time: 7.02491e+07s, dt:22645.9s, Cycle: 1252 +well_1Control: BHP (at the specified reference elevation): 50043947.74368596 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 5.90e-11 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.98e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.62e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 9.61e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.63e-05 ) ; ( Rwell ) = ( 3.66e-15 ) ; ( R ) = ( 3.63e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50049988.033715375 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151874 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243927 +Time: 7.02718e+07s, dt:22645.9s, Cycle: 1253 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.28e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 5.92e-11 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.83e-05 ) ; ( Rwell ) = ( 4.89e-15 ) ; ( R ) = ( 4.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151848 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.002436 +Time: 7.02944e+07s, dt:22645.9s, Cycle: 1254 +well_1Control: BHP (at the specified reference elevation): 50056026.31158057 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.27e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 5.86e-11 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 3.33e-11 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 2.94e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.66e-11 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.09e-05 ) ; ( Rwell ) = ( 3.16e-16 ) ; ( R ) = ( 3.09e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243415 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.0317e+07s, dt:45291.9s, Cycle: 1255 +well_1Control: BHP (at the specified reference elevation): 50062060.4158455 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.26e-09 ) ; ( R ) = ( 3.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.36e-10 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.07e-10 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.83e-10 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.60e-10 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.41e-10 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.39e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.23e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.08e-10 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.24e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.89e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 9.53e-11 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.83e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.36e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.26e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 8.51e-11 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.14e-03 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 9.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 9.16e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.47e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 8.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.02e-03 ) ; ( Rwell ) = ( 8.59e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.43e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 8.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 8.06e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 8.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-03 ) ; ( Rwell ) = ( 7.55e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.72e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.57e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.95e-05 ) ; ( Rwell ) = ( 9.33e-15 ) ; ( R ) = ( 3.95e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0303572 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00488638 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.03623e+07s, dt:22645.9s, Cycle: 1256 +well_1Control: BHP (at the specified reference elevation): 50074120.25669242 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 1.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 5.92e-11 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 3.23e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 9.63e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 8.43e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 7.37e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.36e-05 ) ; ( Rwell ) = ( 7.43e-16 ) ; ( R ) = ( 4.36e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151733 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244755 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.0385e+07s, dt:11323s, Cycle: 1257 +well_1Control: BHP (at the specified reference elevation): 50080152.8845637 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 7.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 7.19e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.36e-05 ) ; ( Rwell ) = ( 1.97e-15 ) ; ( R ) = ( 2.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00758535 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122458 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.03963e+07s, dt:5661.48s, Cycle: 1258 +well_1Control: BHP (at the specified reference elevation): 50083170.02793889 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 4.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.99e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-04 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 8.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50084676.41332367 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00379262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000612432 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.0402e+07s, dt:11323s, Cycle: 1259 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; ( R ) = ( 1.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-05 ) ; ( Rwell ) = ( 1.88e-15 ) ; ( R ) = ( 1.58e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00758621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122546 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.04133e+07s, dt:22645.9s, Cycle: 1260 +well_1Control: BHP (at the specified reference elevation): 50087693.205087505 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 5.87e-11 ) ; ( R ) = ( 4.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.90e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.04e-05 ) ; ( Rwell ) = ( 1.21e-14 ) ; ( R ) = ( 3.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151668 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245176 +Time: 7.04359e+07s, dt:22645.9s, Cycle: 1261 +well_1Control: BHP (at the specified reference elevation): 50093727.42058683 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 5.87e-11 ) ; ( R ) = ( 4.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.33e-11 ) ; ( R ) = ( 3.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 9.27e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.16e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.37e-05 ) ; ( Rwell ) = ( 8.96e-15 ) ; ( R ) = ( 6.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50099761.84129296 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245076 +Time: 7.04586e+07s, dt:22645.9s, Cycle: 1262 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 5.93e-11 ) ; ( R ) = ( 5.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.98e-05 ) ; ( Rwell ) = ( 1.46e-14 ) ; ( R ) = ( 2.98e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50105795.82246303 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244809 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.04812e+07s, dt:45291.9s, Cycle: 1263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 3.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 8.40e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.73e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 4.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.57e-09 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 8.93e-11 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.53e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 5.56e-09 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 2.55e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-03 ) ; ( Rwell ) = ( 5.78e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 9.34e-11 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.16e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.39e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 8.29e-11 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.53e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 7.30e-11 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.71e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.83e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 6.40e-11 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.12e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 5.62e-11 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.50e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.81e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.46e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.95e-11 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.35e-11 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.96e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 8.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 8.40e-05 ) ; ( Rwell ) = ( 8.33e-15 ) ; ( R ) = ( 8.40e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0303152 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00489111 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.05265e+07s, dt:22645.9s, Cycle: 1264 +well_1Control: BHP (at the specified reference elevation): 50117858.41993889 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.90e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 7.75e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 7.26e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 6.81e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 9.58e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.98e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 8.98e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 9.09e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50123888.888184175 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151493 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245214 +Time: 7.05492e+07s, dt:22645.9s, Cycle: 1265 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.24e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 5.83e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 4.47e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.93e-11 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.45e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.82e-05 ) ; ( Rwell ) = ( 8.74e-15 ) ; ( R ) = ( 5.82e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50129917.52079213 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151505 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024581 +Time: 7.05718e+07s, dt:22645.9s, Cycle: 1266 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 5.77e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.59e-05 ) ; ( Rwell ) = ( 1.87e-15 ) ; ( R ) = ( 3.59e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151469 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00246678 +Time: 7.05945e+07s, dt:22645.9s, Cycle: 1267 +well_1Control: BHP (at the specified reference elevation): 50135946.76042035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 5.87e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.63e-05 ) ; ( Rwell ) = ( 2.65e-15 ) ; ( R ) = ( 4.63e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50141975.446364775 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.015144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00247351 +Time: 7.06171e+07s, dt:22645.9s, Cycle: 1268 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 5.90e-11 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.88e-11 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.42e-05 ) ; ( Rwell ) = ( 6.56e-15 ) ; ( R ) = ( 3.42e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.36e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50148003.24843629 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151411 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00247915 +Time: 7.06397e+07s, dt:22645.9s, Cycle: 1269 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.23e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 5.94e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.35e-11 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 8.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151351 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024841 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.06624e+07s, dt:45291.9s, Cycle: 1270 +well_1Control: BHP (at the specified reference elevation): 50154024.88192443 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; ( R ) = ( 3.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 2.33e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 2.05e-10 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.80e-10 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.59e-10 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.27e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.51e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.23e-10 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.71e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.05e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.08e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.31e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 9.48e-11 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.45e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 8.33e-11 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.45e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 7.33e-11 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.44e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.70e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 6.45e-11 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.09e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.67e-11 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.74e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.11e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.99e-11 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.75e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.43e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 4.39e-11 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.73e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.38e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.86e-11 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.68e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.46e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.39e-11 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 9.72e-03 ) ; ( Rwell ) = ( 2.98e-11 ) ; ( R ) = ( 9.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.51e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 9.22e-03 ) ; ( Rwell ) = ( 2.62e-11 ) ; ( R ) = ( 9.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 1.81e-14 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.03027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00497134 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.07077e+07s, dt:22645.9s, Cycle: 1271 +well_1Control: BHP (at the specified reference elevation): 50166071.750474155 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 5.83e-11 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 3.30e-11 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 9.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151238 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00248564 +Time: 7.07303e+07s, dt:22645.9s, Cycle: 1272 +well_1Control: BHP (at the specified reference elevation): 50172091.38043529 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 6.21e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 8.43e-10 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 8.25e-10 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.18e-10 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 4.72e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 9.55e-13 ) ; ( R ) = ( 3.39e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.015127 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024829 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.0753e+07s, dt:45291.9s, Cycle: 1273 +well_1Control: BHP (at the specified reference elevation): 50178117.20547415 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; ( R ) = ( 3.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.32e-10 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.04e-10 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 1.80e-10 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.10e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 1.37e-10 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 7.78e-11 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 8.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 8.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 7.77e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 5.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 7.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 6.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 6.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 9.65e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 9.32e-12 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 6.01e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 9.04e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 8.21e-12 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 5.63e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 8.48e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 9.90e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 5.28e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 7.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 9.28e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 9.94e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.31e-05 ) ; ( Rwell ) = ( 1.19e-14 ) ; ( R ) = ( 1.31e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0302468 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00494707 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.07983e+07s, dt:22645.9s, Cycle: 1274 +well_1Control: BHP (at the specified reference elevation): 50190163.31779009 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.22e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 5.84e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.29e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.90e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 9.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00246856 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.08209e+07s, dt:45291.9s, Cycle: 1275 +well_1Control: BHP (at the specified reference elevation): 50196173.32012174 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 3.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 2.32e-10 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.74e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 2.05e-10 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.80e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.23e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.10e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.08e-10 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 9.52e-11 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.71e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.64e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 8.36e-11 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.18e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.65e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 7.36e-11 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 6.47e-11 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.45e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 5.69e-11 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.99e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 5.01e-11 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.93e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.41e-11 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 3.93e-11 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.74e-04 ) ; ( Rwell ) = ( 2.28e-15 ) ; ( R ) = ( 1.74e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0302319 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0049235 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.08662e+07s, dt:22645.9s, Cycle: 1276 +well_1Control: BHP (at the specified reference elevation): 50208203.947571635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.84e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 8.53e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 8.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50214212.1315293 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151042 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00247 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.08889e+07s, dt:45291.9s, Cycle: 1277 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; ( R ) = ( 3.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.33e-10 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.04e-10 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.16e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.80e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.29e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.38e-10 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.23e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.03e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.72e-03 ) ; ( Rwell ) = ( 6.91e-11 ) ; ( R ) = ( 8.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.13e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 7.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 8.24e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 6.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 7.21e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 6.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 6.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.55e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 5.95e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 8.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 8.09e-12 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.58e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 8.39e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 9.79e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 5.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 5.23e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 7.86e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 9.18e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 9.84e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 4.90e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 7.37e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.61e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 9.22e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 4.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 6.91e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 8.07e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.64e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.31e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 6.48e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 7.56e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 8.10e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.04e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 6.08e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 7.09e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 7.60e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.79e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 5.70e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 6.65e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 7.12e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 22645.93978537619 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 5.86e-11 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 1.09e-14 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00247521 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 22645.93978537619, remaining dt = 22645.93978537619 +well_1Control: BHP (at the specified reference elevation): 50220228.92834258 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 5.89e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 9.58e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.53e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.11e-06 ) ; ( Rwell ) = ( 5.79e-15 ) ; ( R ) = ( 7.11e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151035 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00247889 +Time: 7.09341e+07s, dt:22645.9s, Cycle: 1278 +well_1Control: BHP (at the specified reference elevation): 50226247.35109831 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 5.79e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.28e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 8.84e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 7.77e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.83e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.38e-05 ) ; ( Rwell ) = ( 8.26e-15 ) ; ( R ) = ( 4.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50232265.493791595 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00248173 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.09568e+07s, dt:11323s, Cycle: 1279 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 8.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 7.30e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 4.99e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.96e-05 ) ; ( Rwell ) = ( 2.34e-15 ) ; ( R ) = ( 1.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754885 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00124133 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.09681e+07s, dt:5661.48s, Cycle: 1280 +well_1Control: BHP (at the specified reference elevation): 50235274.88463847 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 4.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 8.31e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50236777.097274736 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00377445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000620725 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.09738e+07s, dt:11323s, Cycle: 1281 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.18e-09 ) ; ( R ) = ( 1.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.09e-05 ) ; ( Rwell ) = ( 2.14e-15 ) ; ( R ) = ( 2.09e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50239786.24356358 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00754974 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00124161 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.09851e+07s, dt:14901.6s, Cycle: 1282 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 7.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 8.99e-12 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 7.92e-12 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.78e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 2.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.39e-05 ) ; ( Rwell ) = ( 3.58e-15 ) ; ( R ) = ( 3.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50243746.47354381 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00993232 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00163393 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.1e+07s, dt:7450.81s, Cycle: 1283 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 5.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 1.31e-12 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049654 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00081684 +compflowStatistics, reservoir: Pressure (min, average, max): 2.99992e+07, 3.00396e+07, 3.01513e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.74977e+07, 1.76499e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.484 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 26.6042, 714.88 } rm^3 +compflowStatistics, reservoir: Phase mass: { 18169, 699585 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2564.23, 217769 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 15604.8, 481816 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.4652, 13.1677 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 18148.5, 699572 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 18169, 0 }, { 2825.84, 696685 } } kg +well_1Control: BHP (at the specified reference elevation): 50245724.820495956 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 2.97912e+07, 2.99387e+07, 3.00178e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.72897e+07, 1.75164e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.526 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.526 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221474 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66442.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155032 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221474 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.000263812, 221474 } } kg +compflowStatistics: Max phase CFL number: 13.7405 +compflowStatistics: Max component CFL number: 18.872 +Time: 7.10075e+07s, dt:7450.81s, Cycle: 1284 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; ( R ) = ( 9.96e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.34e-05 ) ; ( Rwell ) = ( 1.65e-15 ) ; ( R ) = ( 2.34e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496603 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00081668 +Time: 7.10149e+07s, dt:7450.81s, Cycle: 1285 +well_1Control: BHP (at the specified reference elevation): 50247705.323732026 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 6.20e-09 ) ; ( R ) = ( 5.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-04 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 1.71e-12 ) ; ( R ) = ( 9.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000816624 +Time: 7.10224e+07s, dt:7450.81s, Cycle: 1286 +well_1Control: BHP (at the specified reference elevation): 50249682.77451557 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; ( R ) = ( 9.53e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.28e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496315 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000816368 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.10298e+07s, dt:14901.6s, Cycle: 1287 +well_1Control: BHP (at the specified reference elevation): 50251660.654412955 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.19e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 6.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 9.06e-12 ) ; ( R ) = ( 4.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 7.98e-12 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 7.03e-12 ) ; ( R ) = ( 4.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.78e-05 ) ; ( Rwell ) = ( 3.29e-15 ) ; ( R ) = ( 4.78e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00993048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00163134 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.10447e+07s, dt:7450.81s, Cycle: 1288 +well_1Control: BHP (at the specified reference elevation): 50255619.62244977 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 6.19e-09 ) ; ( R ) = ( 5.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.32e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.17e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 1.08e-12 ) ; ( R ) = ( 6.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496336 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000815213 +Time: 7.10522e+07s, dt:7450.81s, Cycle: 1289 +well_1Control: BHP (at the specified reference elevation): 50257596.23560569 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 6.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.07e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 1.68e-12 ) ; ( R ) = ( 9.79e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496211 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000814747 +Time: 7.10596e+07s, dt:7450.81s, Cycle: 1290 +well_1Control: BHP (at the specified reference elevation): 50259570.16650681 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 9.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.49e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 1.16e-15 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049648 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000814349 +Time: 7.10671e+07s, dt:7450.81s, Cycle: 1291 +well_1Control: BHP (at the specified reference elevation): 50261548.45176712 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 5.35e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 9.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000813801 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.10745e+07s, dt:14901.6s, Cycle: 1292 +well_1Control: BHP (at the specified reference elevation): 50263525.41663675 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 7.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.89e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 6.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 8.10e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.53e-05 ) ; ( Rwell ) = ( 3.30e-16 ) ; ( R ) = ( 2.53e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00992608 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00162497 +Time: 7.10894e+07s, dt:14901.6s, Cycle: 1293 +well_1Control: BHP (at the specified reference elevation): 50267479.89816256 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.50e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 6.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.85e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 5.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 5.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 9.45e-12 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 8.32e-12 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 7.36e-12 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 4.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.07e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.28e-05 ) ; ( Rwell ) = ( 6.31e-15 ) ; ( R ) = ( 3.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00992354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00162175 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.11043e+07s, dt:7450.81s, Cycle: 1294 +well_1Control: BHP (at the specified reference elevation): 50271434.69141309 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 5.33e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 9.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000810245 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.11118e+07s, dt:14901.6s, Cycle: 1295 +well_1Control: BHP (at the specified reference elevation): 50273406.28043877 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.15e-09 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 6.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 9.46e-12 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.45e-05 ) ; ( Rwell ) = ( 2.58e-15 ) ; ( R ) = ( 3.45e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00992361 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00161743 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.11267e+07s, dt:7450.81s, Cycle: 1296 +well_1Control: BHP (at the specified reference elevation): 50277361.86570977 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 5.32e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.50e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000809087 +Time: 7.11341e+07s, dt:7450.81s, Cycle: 1297 +well_1Control: BHP (at the specified reference elevation): 50279336.877128586 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 9.54e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.65e-05 ) ; ( Rwell ) = ( 5.12e-15 ) ; ( R ) = ( 1.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.84e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50281314.197492145 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00496114 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000809072 +Time: 7.11416e+07s, dt:7450.81s, Cycle: 1298 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 5.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.07e-04 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.83e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50283289.78302145 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00495913 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000809144 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.1149e+07s, dt:14901.6s, Cycle: 1299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 1.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 6.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.52e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 6.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 5.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.87e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 5.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 9.36e-12 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 4.71e-15 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00991941 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00161807 +Time: 7.11639e+07s, dt:14901.6s, Cycle: 1300 +well_1Control: BHP (at the specified reference elevation): 50287242.25281303 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 1.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 5.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 5.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 9.81e-12 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 8.61e-12 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 7.54e-12 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 6.61e-12 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.06e-05 ) ; ( Rwell ) = ( 2.70e-15 ) ; ( R ) = ( 3.06e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00991706 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00161744 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.11788e+07s, dt:7450.81s, Cycle: 1301 +well_1Control: BHP (at the specified reference elevation): 50291194.559962034 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 5.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.37e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 9.98e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000808459 +Time: 7.11863e+07s, dt:7450.81s, Cycle: 1302 +well_1Control: BHP (at the specified reference elevation): 50293168.7157623 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 9.96e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.70e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.64e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 2.26e-16 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049589 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000808174 +Time: 7.11937e+07s, dt:7450.81s, Cycle: 1303 +well_1Control: BHP (at the specified reference elevation): 50295144.55498019 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 5.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.79e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.50e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.33e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 1.15e-12 ) ; ( R ) = ( 9.39e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50297119.57732112 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00495705 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000807962 +Time: 7.12012e+07s, dt:7450.81s, Cycle: 1304 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 9.36e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 6.54e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.69e-05 ) ; ( Rwell ) = ( 5.65e-16 ) ; ( R ) = ( 2.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.10e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50299095.5371318 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00495784 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000807481 +Time: 7.12086e+07s, dt:7450.81s, Cycle: 1305 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 5.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 1.53e-12 ) ; ( R ) = ( 9.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495639 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080707 +Time: 7.12161e+07s, dt:7450.81s, Cycle: 1306 +well_1Control: BHP (at the specified reference elevation): 50301070.52130406 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 9.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.00e-05 ) ; ( Rwell ) = ( 6.52e-16 ) ; ( R ) = ( 2.00e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000806549 +Time: 7.12235e+07s, dt:7450.81s, Cycle: 1307 +well_1Control: BHP (at the specified reference elevation): 50303046.28109068 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 5.30e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 9.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495525 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000806335 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.1231e+07s, dt:14901.6s, Cycle: 1308 +well_1Control: BHP (at the specified reference elevation): 50305020.53698191 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.84e-03 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 6.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 7.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 9.90e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 8.70e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 7.61e-12 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.86e-05 ) ; ( Rwell ) = ( 3.16e-15 ) ; ( R ) = ( 2.86e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.70e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50308971.69050211 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00991342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0016098 +Time: 7.12459e+07s, dt:14901.6s, Cycle: 1309 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 1.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 6.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 9.24e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.63e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 8.95e-16 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00991017 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160696 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.12608e+07s, dt:7450.81s, Cycle: 1310 +well_1Control: BHP (at the specified reference elevation): 50312923.59573699 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 5.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.00e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.39e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.79e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.36e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 9.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50314897.257788315 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00495403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803011 +Time: 7.12682e+07s, dt:7450.81s, Cycle: 1311 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; ( R ) = ( 9.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.41e-05 ) ; ( Rwell ) = ( 3.07e-15 ) ; ( R ) = ( 2.41e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495623 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000802775 +Time: 7.12757e+07s, dt:7450.81s, Cycle: 1312 +well_1Control: BHP (at the specified reference elevation): 50316872.86485906 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 6.84e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 9.95e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50318845.78655845 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00495347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803361 +Time: 7.12831e+07s, dt:7450.81s, Cycle: 1313 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 6.15e-09 ) ; ( R ) = ( 9.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.99e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.09e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.25e-05 ) ; ( Rwell ) = ( 1.24e-15 ) ; ( R ) = ( 2.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803446 +Time: 7.12906e+07s, dt:7450.81s, Cycle: 1314 +well_1Control: BHP (at the specified reference elevation): 50320822.260317564 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.16e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 9.60e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 9.59e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 9.59e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 9.60e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.60e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 9.60e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 9.61e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 9.61e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 9.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049529 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803666 +Time: 7.1298e+07s, dt:7450.81s, Cycle: 1315 +well_1Control: BHP (at the specified reference elevation): 50322795.17872618 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 9.81e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.72e-05 ) ; ( Rwell ) = ( 1.12e-15 ) ; ( R ) = ( 2.72e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495433 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803876 +Time: 7.13055e+07s, dt:7450.81s, Cycle: 1316 +well_1Control: BHP (at the specified reference elevation): 50324769.94134328 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.43e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.66e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 9.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50326742.40464781 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00495215 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804045 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.13129e+07s, dt:14901.6s, Cycle: 1317 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.98e-03 ) ; ( Rwell ) = ( 2.01e-11 ) ; ( R ) = ( 5.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 5.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 9.38e-12 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 6.42e-12 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 5.05e-12 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.62e-05 ) ; ( Rwell ) = ( 3.38e-15 ) ; ( R ) = ( 4.62e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00990602 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160846 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.13278e+07s, dt:7450.81s, Cycle: 1318 +well_1Control: BHP (at the specified reference elevation): 50330689.76521766 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.82e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.61e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495102 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804331 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.13353e+07s, dt:14901.6s, Cycle: 1319 +well_1Control: BHP (at the specified reference elevation): 50332662.27205465 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 6.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 6.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 6.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.30e-05 ) ; ( Rwell ) = ( 5.99e-15 ) ; ( R ) = ( 4.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00990445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160734 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.13502e+07s, dt:7450.81s, Cycle: 1320 +well_1Control: BHP (at the specified reference elevation): 50336608.901346035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495048 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803622 +Time: 7.13576e+07s, dt:7450.81s, Cycle: 1321 +well_1Control: BHP (at the specified reference elevation): 50338581.56439802 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.78e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.91e-05 ) ; ( Rwell ) = ( 9.73e-16 ) ; ( R ) = ( 1.91e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00495142 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080323 +Time: 7.13651e+07s, dt:7450.81s, Cycle: 1322 +well_1Control: BHP (at the specified reference elevation): 50340555.11031979 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.67e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803005 +Time: 7.13725e+07s, dt:7450.81s, Cycle: 1323 +well_1Control: BHP (at the specified reference elevation): 50342527.99398212 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 9.52e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.84e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 1.47e-12 ) ; ( R ) = ( 9.19e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000802571 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.138e+07s, dt:14901.6s, Cycle: 1324 +well_1Control: BHP (at the specified reference elevation): 50344498.10694408 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 1.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 5.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.33e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 6.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.67e-03 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 5.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 8.57e-12 ) ; ( R ) = ( 5.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 7.59e-12 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 6.72e-12 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 1.39e-15 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.06e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50348446.946537554 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00989955 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160337 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.13949e+07s, dt:7450.81s, Cycle: 1325 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.73e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.97e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.39e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 1.24e-12 ) ; ( R ) = ( 9.80e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494842 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000801096 +Time: 7.14023e+07s, dt:7450.81s, Cycle: 1326 +well_1Control: BHP (at the specified reference elevation): 50350419.4557613 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.77e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 5.73e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 3.51e-15 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494888 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080064 +Time: 7.14098e+07s, dt:7450.81s, Cycle: 1327 +well_1Control: BHP (at the specified reference elevation): 50352394.282980904 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.69e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.39e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 9.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494761 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000799886 +Time: 7.14172e+07s, dt:7450.81s, Cycle: 1328 +well_1Control: BHP (at the specified reference elevation): 50354366.95042518 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.66e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 6.88e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.92e-05 ) ; ( Rwell ) = ( 9.42e-16 ) ; ( R ) = ( 2.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494851 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00079939 +Time: 7.14247e+07s, dt:7450.81s, Cycle: 1329 +well_1Control: BHP (at the specified reference elevation): 50356341.13500204 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.36e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.39e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.68e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 1.50e-12 ) ; ( R ) = ( 9.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494675 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000800347 +Time: 7.14321e+07s, dt:7450.81s, Cycle: 1330 +well_1Control: BHP (at the specified reference elevation): 50358313.42456293 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.56e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.24e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.27e-05 ) ; ( Rwell ) = ( 8.34e-16 ) ; ( R ) = ( 2.27e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494805 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000801081 +Time: 7.14396e+07s, dt:7450.81s, Cycle: 1331 +well_1Control: BHP (at the specified reference elevation): 50360286.96570052 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.39e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.67e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.32e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 1.18e-12 ) ; ( R ) = ( 9.49e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494611 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000801928 +Time: 7.1447e+07s, dt:7450.81s, Cycle: 1332 +well_1Control: BHP (at the specified reference elevation): 50362259.31190336 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.47e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.26e-05 ) ; ( Rwell ) = ( 3.14e-15 ) ; ( R ) = ( 2.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494719 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000802531 +Time: 7.14545e+07s, dt:7450.81s, Cycle: 1333 +well_1Control: BHP (at the specified reference elevation): 50364232.60646275 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.67e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.33e-12 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049454 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803238 +Time: 7.1462e+07s, dt:7450.81s, Cycle: 1334 +well_1Control: BHP (at the specified reference elevation): 50366204.79960546 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.71e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.90e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.19e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.84e-05 ) ; ( Rwell ) = ( 1.14e-15 ) ; ( R ) = ( 1.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.78e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50368177.90743347 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00494671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803698 +Time: 7.14694e+07s, dt:7450.81s, Cycle: 1335 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.14e-09 ) ; ( R ) = ( 5.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.99e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.54e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 9.97e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494471 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080435 +Time: 7.14769e+07s, dt:7450.81s, Cycle: 1336 +well_1Control: BHP (at the specified reference elevation): 50370149.73021583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.28e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.21e-05 ) ; ( Rwell ) = ( 1.71e-15 ) ; ( R ) = ( 2.21e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080468 +Time: 7.14843e+07s, dt:7450.81s, Cycle: 1337 +well_1Control: BHP (at the specified reference elevation): 50372122.32435785 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049441 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000805193 +Time: 7.14918e+07s, dt:7450.81s, Cycle: 1338 +well_1Control: BHP (at the specified reference elevation): 50374093.90286963 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.70e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 1.57e-15 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494555 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000805412 +Time: 7.14992e+07s, dt:7450.81s, Cycle: 1339 +well_1Control: BHP (at the specified reference elevation): 50376066.594843864 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.87e-10 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.85e-10 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.85e-10 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50378038.17590399 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00494324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000805772 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.15067e+07s, dt:14901.6s, Cycle: 1340 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.44e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 6.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 6.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 5.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 6.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 5.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 5.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 8.98e-12 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 7.91e-12 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 6.97e-12 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.97e-05 ) ; ( Rwell ) = ( 2.73e-15 ) ; ( R ) = ( 3.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0098881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00161219 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.15216e+07s, dt:7450.81s, Cycle: 1341 +well_1Control: BHP (at the specified reference elevation): 50381983.5317664 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-04 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 9.48e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50383953.154168695 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00494234 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000806334 +Time: 7.1529e+07s, dt:7450.81s, Cycle: 1342 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 6.12e-09 ) ; ( R ) = ( 9.45e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.99e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 2.69e-12 ) ; ( R ) = ( 9.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000806456 +Time: 7.15365e+07s, dt:7450.81s, Cycle: 1343 +well_1Control: BHP (at the specified reference elevation): 50385924.970209494 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 9.90e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.36e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.64e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.86e-05 ) ; ( Rwell ) = ( 7.12e-16 ) ; ( R ) = ( 1.86e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494471 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000806281 +Time: 7.15439e+07s, dt:7450.81s, Cycle: 1344 +well_1Control: BHP (at the specified reference elevation): 50387897.37347985 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 6.13e-09 ) ; ( R ) = ( 5.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-04 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 1.81e-12 ) ; ( R ) = ( 9.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000806264 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.15514e+07s, dt:14901.6s, Cycle: 1345 +well_1Control: BHP (at the specified reference elevation): 50389867.353649996 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 1.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 6.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 7.88e-12 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 4.74e-12 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.89e-05 ) ; ( Rwell ) = ( 2.10e-15 ) ; ( R ) = ( 4.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00988427 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00161184 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.15663e+07s, dt:7450.81s, Cycle: 1346 +well_1Control: BHP (at the specified reference elevation): 50393810.30805178 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.92e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.46e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50395780.58917849 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00494071 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080534 +Time: 7.15737e+07s, dt:7450.81s, Cycle: 1347 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.92e-05 ) ; ( Rwell ) = ( 7.42e-16 ) ; ( R ) = ( 2.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00494181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804649 +Time: 7.15812e+07s, dt:7450.81s, Cycle: 1348 +well_1Control: BHP (at the specified reference elevation): 50397750.98818883 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.53e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 9.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804466 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.15886e+07s, dt:14901.6s, Cycle: 1349 +well_1Control: BHP (at the specified reference elevation): 50399719.715855464 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 7.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 6.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 6.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 5.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 3.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 7.94e-12 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 7.00e-12 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 6.18e-12 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.06e-05 ) ; ( Rwell ) = ( 3.54e-15 ) ; ( R ) = ( 3.06e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0098814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160683 +Time: 7.16035e+07s, dt:14901.6s, Cycle: 1350 +well_1Control: BHP (at the specified reference elevation): 50403660.46950665 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 1.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 6.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 5.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.84e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 9.08e-12 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 7.89e-12 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 6.24e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.36e-05 ) ; ( Rwell ) = ( 2.14e-15 ) ; ( R ) = ( 3.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50407602.05628519 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00987813 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160469 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.16184e+07s, dt:7450.81s, Cycle: 1351 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.62e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.74e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 8.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50409569.89551008 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00493788 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000801835 +Time: 7.16259e+07s, dt:7450.81s, Cycle: 1352 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 8.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.79e-05 ) ; ( Rwell ) = ( 1.48e-15 ) ; ( R ) = ( 1.79e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50411540.84621194 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00493972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000801085 +Time: 7.16333e+07s, dt:7450.81s, Cycle: 1353 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.99e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.02e-12 ) ; ( R ) = ( 9.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493722 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000800525 +Time: 7.16408e+07s, dt:7450.81s, Cycle: 1354 +well_1Control: BHP (at the specified reference elevation): 50413506.989846334 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 9.61e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 1.32e-12 ) ; ( R ) = ( 9.31e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493667 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000799829 +Time: 7.16482e+07s, dt:7450.81s, Cycle: 1355 +well_1Control: BHP (at the specified reference elevation): 50415475.17373832 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 9.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.49e-05 ) ; ( Rwell ) = ( 1.22e-16 ) ; ( R ) = ( 1.49e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493872 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000798919 +Time: 7.16557e+07s, dt:7450.81s, Cycle: 1356 +well_1Control: BHP (at the specified reference elevation): 50417445.752210826 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.34e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.02e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50419414.51871688 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00493629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000798096 +Time: 7.16631e+07s, dt:7450.81s, Cycle: 1357 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 9.83e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.48e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.17e-05 ) ; ( Rwell ) = ( 4.34e-16 ) ; ( R ) = ( 2.17e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493776 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000798206 +Time: 7.16706e+07s, dt:7450.81s, Cycle: 1358 +well_1Control: BHP (at the specified reference elevation): 50421384.74770011 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 6.43e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.78e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.58e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.41e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 9.75e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493564 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000798937 +Time: 7.1678e+07s, dt:7450.81s, Cycle: 1359 +well_1Control: BHP (at the specified reference elevation): 50423353.85779168 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 9.72e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 9.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00079994 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.16855e+07s, dt:14901.6s, Cycle: 1360 +well_1Control: BHP (at the specified reference elevation): 50425322.8792505 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.25e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 8.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 9.94e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 7.69e-12 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 3.23e-15 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00987261 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160264 +Time: 7.17004e+07s, dt:14901.6s, Cycle: 1361 +well_1Control: BHP (at the specified reference elevation): 50429263.68514493 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 1.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 6.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 6.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 8.77e-12 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 5.98e-12 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.64e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.92e-05 ) ; ( Rwell ) = ( 2.95e-16 ) ; ( R ) = ( 2.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00986922 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160514 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.17153e+07s, dt:7450.81s, Cycle: 1362 +well_1Control: BHP (at the specified reference elevation): 50433205.73545733 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 7.13e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.81e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.61e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.43e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 1.13e-12 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803085 +Time: 7.17227e+07s, dt:7450.81s, Cycle: 1363 +well_1Control: BHP (at the specified reference elevation): 50435175.94417052 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 9.49e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.46e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 5.70e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.04e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.45e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.55e-05 ) ; ( Rwell ) = ( 1.01e-15 ) ; ( R ) = ( 2.55e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493442 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803621 +Time: 7.17302e+07s, dt:7450.81s, Cycle: 1364 +well_1Control: BHP (at the specified reference elevation): 50437146.82479532 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.00e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 9.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803888 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.17376e+07s, dt:14901.6s, Cycle: 1365 +well_1Control: BHP (at the specified reference elevation): 50439114.311041415 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 1.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.36e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 8.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 7.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.48e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 7.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.10e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 7.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.23e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 6.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 5.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 5.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 6.26e-12 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.70e-05 ) ; ( Rwell ) = ( 5.89e-15 ) ; ( R ) = ( 2.70e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00986739 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160867 +Time: 7.17525e+07s, dt:14901.6s, Cycle: 1366 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 50443057.89355409 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 1.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.22e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 5.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 4.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 9.00e-12 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 7.94e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 7.01e-12 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.44e-05 ) ; ( Rwell ) = ( 2.85e-15 ) ; ( R ) = ( 3.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00986439 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160905 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.17674e+07s, dt:7450.81s, Cycle: 1367 +well_1Control: BHP (at the specified reference elevation): 50447001.379259974 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.32e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 1.17e-12 ) ; ( R ) = ( 9.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804709 +Time: 7.17749e+07s, dt:7450.81s, Cycle: 1368 +well_1Control: BHP (at the specified reference elevation): 50448971.89189583 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 9.84e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.66e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.22e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.47e-05 ) ; ( Rwell ) = ( 2.23e-15 ) ; ( R ) = ( 2.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804784 +Time: 7.17823e+07s, dt:7450.81s, Cycle: 1369 +well_1Control: BHP (at the specified reference elevation): 50450944.09944628 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.45e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.99e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-04 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.72e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 9.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493035 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804638 +Time: 7.17898e+07s, dt:7450.81s, Cycle: 1370 +well_1Control: BHP (at the specified reference elevation): 50452912.79785192 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 9.18e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.37e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.56e-05 ) ; ( Rwell ) = ( 2.62e-15 ) ; ( R ) = ( 1.56e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00493253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804752 +Time: 7.17972e+07s, dt:7450.81s, Cycle: 1371 +well_1Control: BHP (at the specified reference elevation): 50454885.36940001 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.85e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 9.73e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000805002 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.18047e+07s, dt:14901.6s, Cycle: 1372 +well_1Control: BHP (at the specified reference elevation): 50456854.83376743 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.30e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 7.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 6.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.50e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 6.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 9.50e-12 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 8.40e-12 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 3.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.61e-05 ) ; ( Rwell ) = ( 5.79e-15 ) ; ( R ) = ( 4.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00986209 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160914 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.18196e+07s, dt:7450.81s, Cycle: 1373 +well_1Control: BHP (at the specified reference elevation): 50460793.88083354 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.65e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.70e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.52e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.36e-12 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049292 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000804225 +Time: 7.1827e+07s, dt:7450.81s, Cycle: 1374 +well_1Control: BHP (at the specified reference elevation): 50462763.05763815 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 9.67e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.51e-05 ) ; ( Rwell ) = ( 8.89e-16 ) ; ( R ) = ( 1.51e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803982 +Time: 7.18345e+07s, dt:7450.81s, Cycle: 1375 +well_1Control: BHP (at the specified reference elevation): 50464732.685995705 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.97e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 9.00e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492836 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803603 +Time: 7.18419e+07s, dt:7450.81s, Cycle: 1376 +well_1Control: BHP (at the specified reference elevation): 50466701.845419005 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 8.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-05 ) ; ( Rwell ) = ( 5.64e-15 ) ; ( R ) = ( 1.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492963 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803439 +Time: 7.18494e+07s, dt:7450.81s, Cycle: 1377 +well_1Control: BHP (at the specified reference elevation): 50468672.00454971 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 9.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492723 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00080312 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.18568e+07s, dt:14901.6s, Cycle: 1378 +well_1Control: BHP (at the specified reference elevation): 50470640.3706052 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 1.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.23e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 7.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.82e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 6.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 2.88e-15 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.07e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50474580.60127345 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00985741 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0016044 +Time: 7.18717e+07s, dt:14901.6s, Cycle: 1379 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 1.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.39e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 6.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.06e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 6.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 7.31e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 1.89e-15 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00985381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160233 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.18866e+07s, dt:7450.81s, Cycle: 1380 +well_1Control: BHP (at the specified reference elevation): 50478521.940257266 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.28e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.17e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.77e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049261 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000800754 +Time: 7.18941e+07s, dt:7450.81s, Cycle: 1381 +well_1Control: BHP (at the specified reference elevation): 50480491.50751986 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.29e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.38e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.30e-05 ) ; ( Rwell ) = ( 9.19e-16 ) ; ( R ) = ( 2.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50482461.55645798 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00492733 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000800008 +Time: 7.19015e+07s, dt:7450.81s, Cycle: 1382 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 4.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.66e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492512 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000799346 +Time: 7.1909e+07s, dt:7450.81s, Cycle: 1383 +well_1Control: BHP (at the specified reference elevation): 50484431.461793534 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 9.78e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.65e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.99e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 5.12e-16 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492682 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000798629 +Time: 7.19164e+07s, dt:7450.81s, Cycle: 1384 +well_1Control: BHP (at the specified reference elevation): 50486401.11448306 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 9.97e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0049245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000798481 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.19239e+07s, dt:14901.6s, Cycle: 1385 +well_1Control: BHP (at the specified reference elevation): 50488370.371846415 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 5.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 9.92e-12 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.74e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 6.11e-16 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00985032 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00159979 +Time: 7.19388e+07s, dt:14901.6s, Cycle: 1386 +well_1Control: BHP (at the specified reference elevation): 50492310.04997313 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 1.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.40e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 7.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 6.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 9.15e-12 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 8.09e-12 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 6.31e-12 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.43e-05 ) ; ( Rwell ) = ( 2.70e-15 ) ; ( R ) = ( 3.43e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.16e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50496249.908887625 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00984789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160236 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.19537e+07s, dt:7450.81s, Cycle: 1387 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 6.70e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.61e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.55e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 1.39e-12 ) ; ( R ) = ( 9.77e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492326 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000801734 +Time: 7.19612e+07s, dt:7450.81s, Cycle: 1388 +well_1Control: BHP (at the specified reference elevation): 50498218.45517433 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-05 ) ; ( Rwell ) = ( 2.51e-15 ) ; ( R ) = ( 1.31e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00492418 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000802192 +Time: 7.19686e+07s, dt:7450.81s, Cycle: 1389 +well_1Control: BHP (at the specified reference elevation): 50500187.88352075 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 5.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.02e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.77e-04 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 1.26e-12 ) ; ( R ) = ( 9.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.08e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50502156.281303346 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00492265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000802689 +Time: 7.19761e+07s, dt:7450.81s, Cycle: 1390 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 9.81e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 9.55e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50504124.19201656 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00492054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000803044 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.19835e+07s, dt:14901.6s, Cycle: 1391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 1.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 4.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 9.32e-12 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 7.80e-12 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 3.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.05e-12 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 5.33e-12 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.28e-05 ) ; ( Rwell ) = ( 6.68e-15 ) ; ( R ) = ( 4.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50508061.51692626 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00984736 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00160707 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.19984e+07s, dt:1591.5s, Cycle: 1392 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.13e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 1.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-04 ) ; ( Rwell ) = ( 1.67e-13 ) ; ( R ) = ( 2.15e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50508482.154007375 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00106298 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000171677 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.2e+07s, dt:3183.01s, Cycle: 1393 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 4.32e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 1.35e-12 ) ; ( R ) = ( 6.40e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50509321.97329804 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0021114 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000343377 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 3.01961e+07, 3.02366e+07, 3.03484e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.76955e+07, 1.78478e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.627 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 26.8979, 714.73 } rm^3 +compflowStatistics, reservoir: Phase mass: { 18431.4, 699544 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2597.85, 217845 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 15833.5, 481699 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.2849, 13.3781 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 18411.1, 699530 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 18431.4, 0 }, { 2857.87, 696611 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 2.99887e+07, 3.01358e+07, 3.02148e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.7488e+07, 1.77142e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.57 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.57 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221548 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66464.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155084 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221548 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.00068857, 221548 } } kg +compflowStatistics: Max phase CFL number: 5.84931 +compflowStatistics: Max component CFL number: 8.03338 +Time: 7.20032e+07s, dt:6366.02s, Cycle: 1394 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; ( R ) = ( 1.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.53e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.38e-12 ) ; ( R ) = ( 9.67e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00420576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000686777 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.20095e+07s, dt:12732s, Cycle: 1395 +well_1Control: BHP (at the specified reference elevation): 50511002.114045635 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.07e-09 ) ; ( R ) = ( 1.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 9.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 8.44e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.76e-05 ) ; ( Rwell ) = ( 3.21e-15 ) ; ( R ) = ( 2.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00841123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00137366 +Time: 7.20223e+07s, dt:12732s, Cycle: 1396 +well_1Control: BHP (at the specified reference elevation): 50514365.432391874 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 9.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 8.92e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 7.85e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.83e-05 ) ; ( Rwell ) = ( 3.05e-15 ) ; ( R ) = ( 2.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00840854 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00137363 +Time: 7.2035e+07s, dt:12732s, Cycle: 1397 +well_1Control: BHP (at the specified reference elevation): 50517730.19331679 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 9.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 9.30e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 8.21e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.25e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.41e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.93e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 3.20e-15 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00840756 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00137281 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.20477e+07s, dt:6366.02s, Cycle: 1398 +well_1Control: BHP (at the specified reference elevation): 50521095.275271416 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 4.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.70e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.63e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 6.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50522777.15330882 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00420318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000686074 +Time: 7.20541e+07s, dt:6366.02s, Cycle: 1399 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 6.59e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 5.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 5.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.88e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.36e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.83e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 1.48e-12 ) ; ( R ) = ( 9.06e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50524455.58137519 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00420269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000686015 +Time: 7.20605e+07s, dt:6366.02s, Cycle: 1400 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 6.05e-09 ) ; ( R ) = ( 9.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 5.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.55e-05 ) ; ( Rwell ) = ( 1.62e-15 ) ; ( R ) = ( 1.55e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00420548 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000685779 +Time: 7.20668e+07s, dt:6366.02s, Cycle: 1401 +well_1Control: BHP (at the specified reference elevation): 50526135.27933185 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 6.06e-09 ) ; ( R ) = ( 4.51e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 9.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00420276 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000685736 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.20732e+07s, dt:12732s, Cycle: 1402 +well_1Control: BHP (at the specified reference elevation): 50527814.80569662 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.56e-06 ) ; ( Rwell ) = ( 1.52e-15 ) ; ( R ) = ( 9.56e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00840718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00137027 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.20859e+07s, dt:25464.1s, Cycle: 1403 +well_1Control: BHP (at the specified reference elevation): 50531175.76267169 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; ( R ) = ( 1.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.27e-11 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.72e-05 ) ; ( Rwell ) = ( 2.04e-14 ) ; ( R ) = ( 3.72e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0168077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00273845 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.21114e+07s, dt:50928.1s, Cycle: 1404 +well_1Control: BHP (at the specified reference elevation): 50537899.27899629 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; ( R ) = ( 3.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 2.85e-10 ) ; ( R ) = ( 9.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.31e-03 ) ; ( Rwell ) = ( 1.61e-10 ) ; ( R ) = ( 6.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.41e-10 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.94e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 7.01e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 6.16e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 5.41e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.18e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.68e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.23e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.55e-05 ) ; ( Rwell ) = ( 1.84e-14 ) ; ( R ) = ( 3.55e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0336067 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0054581 +Time: 7.21623e+07s, dt:50928.1s, Cycle: 1405 +well_1Control: BHP (at the specified reference elevation): 50551338.78088006 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; ( R ) = ( 3.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 2.85e-10 ) ; ( R ) = ( 7.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 7.17e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.05e-05 ) ; ( Rwell ) = ( 3.10e-14 ) ; ( R ) = ( 6.05e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0335925 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00542188 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.22133e+07s, dt:101856s, Cycle: 1406 +well_1Control: BHP (at the specified reference elevation): 50564778.31203163 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 6.06e-09 ) ; ( R ) = ( 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 9.92e-09 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.31e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 9.68e-09 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 9.57e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 9.43e-09 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.22e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.38e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 9.40e-09 ) ; ( R ) = ( 7.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.84e-04 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 2.84e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.86e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50591620.541204184 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.067149 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.010764 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.23151e+07s, dt:203713s, Cycle: 1407 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.04e-09 ) ; ( R ) = ( 1.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 4.47e-09 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 5.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.73e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; ( R ) = ( 9.73e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 3.54e-09 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 4.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 3.14e-09 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.40e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 4.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.26e-02 ) ; ( Rwell ) = ( 8.51e-10 ) ; ( R ) = ( 8.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 6.50e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 7.18e-10 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 5.81e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 6.44e-10 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 5.52e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 9.70e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 5.95e-10 ) ; ( R ) = ( 6.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 5.23e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 9.09e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 5.50e-10 ) ; ( R ) = ( 6.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.95e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 8.53e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 5.09e-10 ) ; ( R ) = ( 6.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 4.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 8.00e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 9.51e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 4.77e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.03e-04 ) ; ( Rwell ) = ( 3.68e-13 ) ; ( R ) = ( 2.03e-04 ) ; + Last LinSolve(iter,res) = ( 11, 6.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.134121 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0216869 +Time: 7.25188e+07s, dt:203713s, Cycle: 1408 +well_1Control: BHP (at the specified reference elevation): 50645166.18121217 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 6.01e-09 ) ; ( R ) = ( 1.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 4.43e-09 ) ; ( R ) = ( 1.35e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 5.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 1.98e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 5.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.79e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; ( R ) = ( 8.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.62e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 8.62e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 6.73e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 4.81e-13 ) ; ( R ) = ( 6.66e-04 ) ; + Last LinSolve(iter,res) = ( 10, 7.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50698696.331594266 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.133848 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0217322 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.27225e+07s, dt:277457s, Cycle: 1409 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 6.00e-09 ) ; ( R ) = ( 1.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.27e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; ( R ) = ( 7.27e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.26e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.61e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 8.89e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.07e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 3.89e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 4.76e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 7.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.03e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.53e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 4.30e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.57e-09 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 6.78e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 9.93e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 3.20e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.89e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 3.15e-09 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 5.93e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 9.48e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 2.91e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 4.59e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 6.73e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 2.17e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.64e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 4.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 6.48e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.97e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 2.39e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 8, 1.00e-02 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 3.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 6.23e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.80e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.17e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.03e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 5.96e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.64e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.97e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 9, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.63e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 5.71e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.49e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 2.90e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.02e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 4.28e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 1.13e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 8.50e-10 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 1.56e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 3.19e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 8.60e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.03e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 7.47e-10 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.35e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 3.06e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 7.85e-11 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 9.37e-11 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 6.57e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 1.31e-13 ) ; ( R ) = ( 5.05e-04 ) ; + Last LinSolve(iter,res) = ( 11, 6.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 50771459.68891856 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.181877 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.029458 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.3e+07s, dt:138728s, Cycle: 1410 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.71e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; ( R ) = ( 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 5.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 6.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 2.06e-11 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.66e-03 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 9.32e-10 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 8.19e-10 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 6.28e-10 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 5.54e-10 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 9.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 4.25e-10 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 8.71e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 3.73e-10 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 8.22e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 3.28e-10 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 7.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 2.89e-10 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 4.57e-14 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0907418 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0145839 +compflowStatistics, reservoir: Pressure (min, average, max): 3.042e+07, 3.04604e+07, 3.05724e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.78926e+07, 1.80451e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.79 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 27.23, 714.56 } rm^3 +compflowStatistics, reservoir: Phase mass: { 18729.2, 699498 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2637.17, 217931 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 16092, 481567 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.4754, 14.3623 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 18708.7, 699484 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 18729.2, 0 }, { 2895.82, 696527 } } kg +well_1Control: BHP (at the specified reference elevation): 50807924.35105783 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 3.02132e+07, 3.03599e+07, 3.04387e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.76858e+07, 1.79113e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.62 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.62 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221632 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66489.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155143 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221632 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.00182945, 221632 } } kg +compflowStatistics: Max phase CFL number: 253.932 +compflowStatistics: Max component CFL number: 348.727 +Time: 7.31387e+07s, dt:138728s, Cycle: 1411 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 5.97e-09 ) ; ( R ) = ( 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.43e-03 ) ; ( Rwell ) = ( 5.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 9.41e-10 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 8.27e-10 ) ; ( R ) = ( 3.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 2.08e-10 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 7.78e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 5.23e-11 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.06e-05 ) ; ( Rwell ) = ( 7.66e-14 ) ; ( R ) = ( 2.06e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0906385 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0146142 +Time: 7.32775e+07s, dt:138728s, Cycle: 1412 +well_1Control: BHP (at the specified reference elevation): 50844361.399543874 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-03 ) ; ( Rwell ) = ( 5.95e-09 ) ; ( R ) = ( 9.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.32e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; ( R ) = ( 9.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 9.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.04e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; ( R ) = ( 4.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.69e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 6.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 9.45e-10 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 8.31e-10 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 7.31e-10 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 6.43e-10 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.47e-04 ) ; ( Rwell ) = ( 3.42e-13 ) ; ( R ) = ( 2.47e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0905436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0144325 +Time: 7.34162e+07s, dt:138728s, Cycle: 1413 +well_1Control: BHP (at the specified reference elevation): 50880768.27494429 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.56e-03 ) ; ( Rwell ) = ( 5.93e-09 ) ; ( R ) = ( 9.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.36e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; ( R ) = ( 8.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.46e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.82e-02 ) ; ( Rwell ) = ( 5.20e-09 ) ; ( R ) = ( 7.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 4.66e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.19e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.22e-05 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 9.22e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0904483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0143047 +Time: 7.35549e+07s, dt:138728s, Cycle: 1414 +well_1Control: BHP (at the specified reference elevation): 50917146.64488252 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 5.92e-09 ) ; ( R ) = ( 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 7.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 6.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 6.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 4.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 9.31e-10 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 8.17e-10 ) ; ( R ) = ( 5.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 7.19e-10 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 6.32e-10 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 5.56e-10 ) ; ( R ) = ( 3.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 4.89e-10 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.30e-10 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.56e-05 ) ; ( Rwell ) = ( 4.50e-14 ) ; ( R ) = ( 7.56e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0903545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0143042 +Time: 7.36936e+07s, dt:138728s, Cycle: 1415 +well_1Control: BHP (at the specified reference elevation): 50953491.493504465 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.46e-03 ) ; ( Rwell ) = ( 5.90e-09 ) ; ( R ) = ( 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.86e-03 ) ; ( Rwell ) = ( 5.53e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 9.52e-09 ) ; ( R ) = ( 6.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-03 ) ; ( Rwell ) = ( 5.17e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.81e-02 ) ; ( Rwell ) = ( 9.33e-09 ) ; ( R ) = ( 7.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 9.14e-09 ) ; ( R ) = ( 7.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 8.97e-09 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 8.83e-09 ) ; ( R ) = ( 5.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 8.70e-09 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 8.59e-09 ) ; ( R ) = ( 4.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 8.50e-09 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 6.53e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.81e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.66e-05 ) ; ( Rwell ) = ( 1.11e-13 ) ; ( R ) = ( 6.66e-05 ) ; + Last LinSolve(iter,res) = ( 8, 1.00e-02 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0902562 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0142751 +Time: 7.38324e+07s, dt:138728s, Cycle: 1416 +well_1Control: BHP (at the specified reference elevation): 50989807.59667885 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.44e-03 ) ; ( Rwell ) = ( 5.89e-09 ) ; ( R ) = ( 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 6.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 8.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 9.22e-10 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 8.11e-10 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 7.13e-10 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.79e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 7.30e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.01e-10 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.51e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 8.57e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 8.88e-11 ) ; ( R ) = ( 6.37e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.44e-05 ) ; ( Rwell ) = ( 3.29e-14 ) ; ( R ) = ( 5.44e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0901556 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0141411 +Time: 7.39711e+07s, dt:28900.6s, Cycle: 1417 +well_1Control: BHP (at the specified reference elevation): 51026074.05297685 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 1.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 8.77e-11 ) ; ( R ) = ( 7.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 6.72e-11 ) ; ( R ) = ( 7.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 5.94e-11 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 5.23e-11 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 4.59e-11 ) ; ( R ) = ( 6.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 4.05e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 3.57e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 3.14e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.02e-05 ) ; ( Rwell ) = ( 1.03e-15 ) ; ( R ) = ( 5.02e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0187636 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00293772 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.4e+07s, dt:14450.3s, Cycle: 1418 +well_1Control: BHP (at the specified reference elevation): 51033643.61693995 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 1.79e-11 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 9.14e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 8.06e-12 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 9.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.74e-05 ) ; ( Rwell ) = ( 6.75e-16 ) ; ( R ) = ( 1.74e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00937982 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146975 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +compflowStatistics, reservoir: Pressure (min, average, max): 3.05926e+07, 3.0633e+07, 3.07451e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.80897e+07, 1.82423e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 741.916 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 27.4864, 714.429 } rm^3 +compflowStatistics, reservoir: Phase mass: { 18959.6, 699463 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2666.91, 217998 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 16292.7, 481465 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.838, 14.5106 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 18938.7, 699448 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 18959.6, 0 }, { 2924.37, 696462 } } kg +well_1Control: BHP (at the specified reference elevation): 51037429.59460881 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 3.0386e+07, 3.05325e+07, 3.06113e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.78831e+07, 1.81084e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.658 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.658 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221697 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66509.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155188 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221697 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.00358268, 221697 } } kg +compflowStatistics: Max phase CFL number: 26.3709 +compflowStatistics: Max component CFL number: 36.2137 +Time: 7.40145e+07s, dt:7225.15s, Cycle: 1419 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 4.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 4.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 9.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51039320.5736862 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00468892 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000735761 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.40217e+07s, dt:14450.3s, Cycle: 1420 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 4.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 9.50e-12 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 8.39e-12 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 6.58e-12 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.77e-05 ) ; ( Rwell ) = ( 5.66e-15 ) ; ( R ) = ( 3.77e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00937995 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147476 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.40361e+07s, dt:7225.15s, Cycle: 1421 +well_1Control: BHP (at the specified reference elevation): 51043105.68725138 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 4.86e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 7.09e-10 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 7.07e-10 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 7.07e-10 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 7.07e-10 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.06e-10 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.70e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.81e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.45e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.30e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.35e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.19e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 1.07e-12 ) ; ( R ) = ( 9.88e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51044997.333904505 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0046885 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00073824 +Time: 7.40434e+07s, dt:7225.15s, Cycle: 1422 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 9.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.76e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.37e-05 ) ; ( Rwell ) = ( 4.22e-16 ) ; ( R ) = ( 1.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000738934 +Time: 7.40506e+07s, dt:7225.15s, Cycle: 1423 +well_1Control: BHP (at the specified reference elevation): 51046889.57261416 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 4.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-04 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.04e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.45e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.31e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.18e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.07e-12 ) ; ( R ) = ( 9.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468804 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000739634 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.40578e+07s, dt:3612.58s, Cycle: 1424 +well_1Control: BHP (at the specified reference elevation): 51048780.84163204 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 4.82e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 5.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00235171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000370056 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.40614e+07s, dt:7225.15s, Cycle: 1425 +well_1Control: BHP (at the specified reference elevation): 51049725.72730879 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 1.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 6.18e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.60e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 1.44e-12 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000740509 +Time: 7.40686e+07s, dt:7225.15s, Cycle: 1426 +well_1Control: BHP (at the specified reference elevation): 51051615.83603953 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 9.83e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.27e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.39e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.95e-05 ) ; ( Rwell ) = ( 1.41e-15 ) ; ( R ) = ( 1.95e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468888 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741076 +Time: 7.40759e+07s, dt:7225.15s, Cycle: 1427 +well_1Control: BHP (at the specified reference elevation): 51053507.68001641 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 4.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741363 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.40831e+07s, dt:14450.3s, Cycle: 1428 +well_1Control: BHP (at the specified reference elevation): 51055397.68551286 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 5.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 4.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 8.97e-12 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 6.95e-12 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 4.76e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.52e-05 ) ; ( Rwell ) = ( 5.61e-15 ) ; ( R ) = ( 4.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51059177.33667202 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00937614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148499 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.40975e+07s, dt:7225.15s, Cycle: 1429 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 4.90e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.37e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.08e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.82e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.93e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 1.52e-12 ) ; ( R ) = ( 8.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468599 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742868 +Time: 7.41048e+07s, dt:7225.15s, Cycle: 1430 +well_1Control: BHP (at the specified reference elevation): 51061066.78075961 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 8.69e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.72e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.57e-05 ) ; ( Rwell ) = ( 4.44e-16 ) ; ( R ) = ( 1.57e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00469043 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074326 +Time: 7.4112e+07s, dt:7225.15s, Cycle: 1431 +well_1Control: BHP (at the specified reference elevation): 51062957.11749835 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-04 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.84e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.00e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 1.55e-12 ) ; ( R ) = ( 9.12e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468536 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743456 +Time: 7.41192e+07s, dt:7225.15s, Cycle: 1432 +well_1Control: BHP (at the specified reference elevation): 51064846.409978785 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.67e-05 ) ; ( Rwell ) = ( 7.72e-16 ) ; ( R ) = ( 1.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743795 +Time: 7.41264e+07s, dt:7225.15s, Cycle: 1433 +well_1Control: BHP (at the specified reference elevation): 51066736.94984095 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.08e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.55e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.10e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.77e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744084 +Time: 7.41337e+07s, dt:7225.15s, Cycle: 1434 +well_1Control: BHP (at the specified reference elevation): 51068626.77594348 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 6.14e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.73e-05 ) ; ( Rwell ) = ( 1.63e-15 ) ; ( R ) = ( 1.73e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074413 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.41409e+07s, dt:14450.3s, Cycle: 1435 +well_1Control: BHP (at the specified reference elevation): 51070517.01796189 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.84e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 5.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.86e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 7.79e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.04e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.58e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 9.72e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 9.12e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 8.55e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 7225.152858510613 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.09e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.21e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.50e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.60e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.43e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 1.29e-12 ) ; ( R ) = ( 9.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468443 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744058 +coupledFlowAndWells: sub-step = 0, accepted dt = 7225.152858510613, remaining dt = 7225.152858510613 +well_1Control: BHP (at the specified reference elevation): 51072406.985163584 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.81e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.82e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.93e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.05e-05 ) ; ( Rwell ) = ( 1.36e-15 ) ; ( R ) = ( 2.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468558 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744098 +Time: 7.41553e+07s, dt:7225.15s, Cycle: 1436 +well_1Control: BHP (at the specified reference elevation): 51074297.40084789 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 9.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744194 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.41626e+07s, dt:14450.3s, Cycle: 1437 +well_1Control: BHP (at the specified reference elevation): 51076187.87209593 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 7.82e-12 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 6.88e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 6.06e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.26e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 4.45e-15 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.37e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51079968.800532565 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00936932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148803 +Time: 7.4177e+07s, dt:14450.3s, Cycle: 1438 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 9.57e-12 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 5.27e-12 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 9.72e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 9.11e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 8.54e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 7225.152858510613 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.07e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.65e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.48e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.33e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.19e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.07e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074392 +coupledFlowAndWells: sub-step = 0, accepted dt = 7225.152858510613, remaining dt = 7225.152858510613 +well_1Control: BHP (at the specified reference elevation): 51081859.132619515 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.58e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.99e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.77e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.58e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.63e-05 ) ; ( Rwell ) = ( 2.14e-15 ) ; ( R ) = ( 1.63e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074372 +Time: 7.41915e+07s, dt:7225.15s, Cycle: 1439 +well_1Control: BHP (at the specified reference elevation): 51083749.32593566 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.13e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.01e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.93e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 9.33e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743618 +Time: 7.41987e+07s, dt:7225.15s, Cycle: 1440 +well_1Control: BHP (at the specified reference elevation): 51085639.26411416 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.96e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 9.65e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743263 +Time: 7.42059e+07s, dt:7225.15s, Cycle: 1441 +well_1Control: BHP (at the specified reference elevation): 51087528.15920202 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.63e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.05e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.79e-05 ) ; ( Rwell ) = ( 2.22e-17 ) ; ( R ) = ( 1.79e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468923 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743062 +Time: 7.42131e+07s, dt:7225.15s, Cycle: 1442 +well_1Control: BHP (at the specified reference elevation): 51089417.979685895 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.74e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 9.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742617 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.42204e+07s, dt:14450.3s, Cycle: 1443 +well_1Control: BHP (at the specified reference elevation): 51091307.482756615 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 1.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 5.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.44e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 5.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 6.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.13e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 5.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 4.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 4.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 6.59e-12 ) ; ( R ) = ( 4.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.84e-12 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 3.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.95e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.93e-05 ) ; ( Rwell ) = ( 4.12e-15 ) ; ( R ) = ( 3.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00936604 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148442 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.42348e+07s, dt:7225.15s, Cycle: 1444 +well_1Control: BHP (at the specified reference elevation): 51095088.19149643 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.68e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.50e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 1.40e-12 ) ; ( R ) = ( 8.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741867 +Time: 7.4242e+07s, dt:7225.15s, Cycle: 1445 +well_1Control: BHP (at the specified reference elevation): 51096977.97564229 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 8.68e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 4.20e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.73e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 1.40e-15 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51098868.66042757 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00468258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741519 +Time: 7.42493e+07s, dt:7225.15s, Cycle: 1446 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.33e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.26e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.12e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 1.00e-12 ) ; ( R ) = ( 9.90e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741118 +Time: 7.42565e+07s, dt:7225.15s, Cycle: 1447 +well_1Control: BHP (at the specified reference elevation): 51100759.06874828 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.77e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 5.15e-16 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468478 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000740669 +Time: 7.42637e+07s, dt:7225.15s, Cycle: 1448 +well_1Control: BHP (at the specified reference elevation): 51102650.182309814 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.55e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.36e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.21e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.09e-04 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.09e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 9.53e-13 ) ; ( R ) = ( 9.13e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468008 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741184 +Time: 7.42709e+07s, dt:7225.15s, Cycle: 1449 +well_1Control: BHP (at the specified reference elevation): 51104540.5889117 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.10e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.69e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.90e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.67e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.36e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 1.96e-15 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51106431.88609572 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00468345 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741799 +Time: 7.42782e+07s, dt:7225.15s, Cycle: 1450 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.93e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.30e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.70e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.73e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 9.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467973 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742463 +Time: 7.42854e+07s, dt:7225.15s, Cycle: 1451 +well_1Control: BHP (at the specified reference elevation): 51108321.59060387 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.62e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.10e-05 ) ; ( Rwell ) = ( 1.12e-15 ) ; ( R ) = ( 2.10e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742942 +Time: 7.42926e+07s, dt:7225.15s, Cycle: 1452 +well_1Control: BHP (at the specified reference elevation): 51110212.27550769 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 4.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-04 ) ; ( Rwell ) = ( 4.67e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.92e-04 ) ; ( Rwell ) = ( 2.15e-12 ) ; ( R ) = ( 9.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467924 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074365 +Time: 7.42998e+07s, dt:7225.15s, Cycle: 1453 +well_1Control: BHP (at the specified reference elevation): 51112100.83861704 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.19e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.33e-06 ) ; ( Rwell ) = ( 3.73e-16 ) ; ( R ) = ( 9.33e-06 ) ; + Last LinSolve(iter,res) = ( 7, 3.89e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51113992.1710099 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00468377 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743931 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.43071e+07s, dt:14450.3s, Cycle: 1454 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 9.82e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 9.05e-12 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.39e-05 ) ; ( Rwell ) = ( 2.08e-15 ) ; ( R ) = ( 3.39e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51117774.47571172 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00935853 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148948 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.43215e+07s, dt:7225.15s, Cycle: 1455 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.22e-04 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.02e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.41e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51119664.39476736 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00467863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745101 +Time: 7.43287e+07s, dt:7225.15s, Cycle: 1456 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 9.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 7.85e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.16e-05 ) ; ( Rwell ) = ( 9.11e-15 ) ; ( R ) = ( 2.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468212 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745351 +Time: 7.4336e+07s, dt:7225.15s, Cycle: 1457 +well_1Control: BHP (at the specified reference elevation): 51121554.96326475 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.86e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.56e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.04e-04 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-04 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.23e-04 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.97e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.76e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.57e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.40e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 9.80e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467815 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745573 +Time: 7.43432e+07s, dt:7225.15s, Cycle: 1458 +well_1Control: BHP (at the specified reference elevation): 51123443.29035383 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.78e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.73e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.63e-05 ) ; ( Rwell ) = ( 1.69e-15 ) ; ( R ) = ( 1.63e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467904 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745767 +Time: 7.43504e+07s, dt:7225.15s, Cycle: 1459 +well_1Control: BHP (at the specified reference elevation): 51125333.49193263 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.36e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.39e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.44e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.29e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467748 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745939 +Time: 7.43576e+07s, dt:7225.15s, Cycle: 1460 +well_1Control: BHP (at the specified reference elevation): 51127221.24440013 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 9.54e-16 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467892 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745977 +Time: 7.43649e+07s, dt:7225.15s, Cycle: 1461 +well_1Control: BHP (at the specified reference elevation): 51129111.34267368 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.88e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.55e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 9.68e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51131000.524184525 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00467708 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000746202 +Time: 7.43721e+07s, dt:7225.15s, Cycle: 1462 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 9.66e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 6.07e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 5.26e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.58e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.93e-05 ) ; ( Rwell ) = ( 2.56e-15 ) ; ( R ) = ( 1.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.24e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51132889.67391115 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00467835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074603 +Time: 7.43793e+07s, dt:7225.15s, Cycle: 1463 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.58e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.19e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 9.61e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51134777.099742755 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00467639 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074586 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.43865e+07s, dt:14450.3s, Cycle: 1464 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 9.46e-12 ) ; ( R ) = ( 4.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 8.36e-12 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 7.39e-12 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.54e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.09e-05 ) ; ( Rwell ) = ( 3.26e-15 ) ; ( R ) = ( 3.09e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.07e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51138555.81684608 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00935528 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00149153 +Time: 7.4401e+07s, dt:14450.3s, Cycle: 1465 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 9.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 6.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 8.94e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 7.89e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 6.97e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.80e-12 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 1.20e-12 ) ; ( R ) = ( 9.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00935106 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00149086 +Time: 7.44154e+07s, dt:14450.3s, Cycle: 1466 +well_1Control: BHP (at the specified reference elevation): 51142332.35870809 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 6.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 6.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 5.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 4.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 4.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 7.96e-12 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.26e-05 ) ; ( Rwell ) = ( 1.76e-15 ) ; ( R ) = ( 2.26e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00935219 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148974 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.44299e+07s, dt:7225.15s, Cycle: 1467 +well_1Control: BHP (at the specified reference elevation): 51146112.395531505 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.94e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.24e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 9.90e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046744 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744273 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.44371e+07s, dt:14450.3s, Cycle: 1468 +well_1Control: BHP (at the specified reference elevation): 51147999.258712575 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 5.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 9.02e-12 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 7.95e-12 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 7.50e-12 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 6.64e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 5.90e-12 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.11e-05 ) ; ( Rwell ) = ( 1.22e-15 ) ; ( R ) = ( 2.11e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.59e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51151777.961839445 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00935295 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148778 +Time: 7.44516e+07s, dt:14450.3s, Cycle: 1469 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 9.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 6.37e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.38e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 1.06e-15 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.31e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51155556.93419589 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00934932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148765 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.4466e+07s, dt:7225.15s, Cycle: 1470 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.13e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.62e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 9.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467394 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743923 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.44732e+07s, dt:14450.3s, Cycle: 1471 +well_1Control: BHP (at the specified reference elevation): 51157442.056246035 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 5.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 5.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.79e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 4.85e-12 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 4.28e-12 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.54e-05 ) ; ( Rwell ) = ( 5.23e-16 ) ; ( R ) = ( 3.54e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00935009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148671 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.44877e+07s, dt:7225.15s, Cycle: 1472 +well_1Control: BHP (at the specified reference elevation): 51161221.24111954 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.84e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.37e-04 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.83e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.97e-04 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.43e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.77e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 9.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743078 +Time: 7.44949e+07s, dt:7225.15s, Cycle: 1473 +well_1Control: BHP (at the specified reference elevation): 51163109.388905786 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.80e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 5.57e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 5.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.30e-05 ) ; ( Rwell ) = ( 2.35e-16 ) ; ( R ) = ( 2.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467525 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742846 +Time: 7.45021e+07s, dt:7225.15s, Cycle: 1474 +well_1Control: BHP (at the specified reference elevation): 51164997.87254966 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.84e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.04e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.81e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.61e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.47e-04 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.43e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-04 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 1.28e-12 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742391 +Time: 7.45094e+07s, dt:7225.15s, Cycle: 1475 +well_1Control: BHP (at the specified reference elevation): 51166885.84693274 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.72e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 5.55e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 4.93e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.48e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.10e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 1.24e-15 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742083 +Time: 7.45166e+07s, dt:7225.15s, Cycle: 1476 +well_1Control: BHP (at the specified reference elevation): 51168774.48085034 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 5.93e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.04e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 2.41e-12 ) ; ( R ) = ( 9.97e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51170661.38949391 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.004672 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741501 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.45238e+07s, dt:14450.3s, Cycle: 1477 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 5.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 4.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 4.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 9.20e-12 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 8.12e-12 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 7.17e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.46e-05 ) ; ( Rwell ) = ( 2.43e-15 ) ; ( R ) = ( 2.46e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00934729 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148136 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.45383e+07s, dt:7225.15s, Cycle: 1478 +well_1Control: BHP (at the specified reference elevation): 51174438.02551614 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.07e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.45e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-04 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-04 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.07e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.35e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.61e-04 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 1.87e-12 ) ; ( R ) = ( 9.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000740064 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.45455e+07s, dt:14450.3s, Cycle: 1479 +well_1Control: BHP (at the specified reference elevation): 51176325.17990227 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 1.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 4.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 4.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 5.85e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.99e-05 ) ; ( Rwell ) = ( 8.91e-16 ) ; ( R ) = ( 2.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00934568 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0014778 +Time: 7.45599e+07s, dt:14450.3s, Cycle: 1480 +well_1Control: BHP (at the specified reference elevation): 51180102.413421206 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.83e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 7.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 4.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 7.86e-12 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 6.93e-12 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 6.11e-12 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.74e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.03e-06 ) ; ( Rwell ) = ( 2.43e-15 ) ; ( R ) = ( 6.03e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00934298 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147498 +Time: 7.45744e+07s, dt:14450.3s, Cycle: 1481 +well_1Control: BHP (at the specified reference elevation): 51183880.746450484 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.81e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 4.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 9.11e-12 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 7.10e-12 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 6.27e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 5.54e-12 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.63e-12 ) ; ( R ) = ( 8.11e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00934229 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147195 +Time: 7.45888e+07s, dt:14450.3s, Cycle: 1482 +well_1Control: BHP (at the specified reference elevation): 51187656.61522712 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 9.80e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 2.14e-11 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 5.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 8.66e-12 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 7.65e-12 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 6.76e-12 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.67e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 6.38e-16 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.42e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51191432.46425074 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00934438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146833 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.46033e+07s, dt:7225.15s, Cycle: 1483 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.88e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.75e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.06e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 1.34e-12 ) ; ( R ) = ( 9.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466982 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000733117 +Time: 7.46105e+07s, dt:7225.15s, Cycle: 1484 +well_1Control: BHP (at the specified reference elevation): 51193318.822303124 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.27e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.64e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.64e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 9.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51195203.80493553 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00466809 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000732334 +Time: 7.46178e+07s, dt:7225.15s, Cycle: 1485 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 9.74e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.68e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.92e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 4.43e-18 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00468277 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000732239 +Time: 7.4625e+07s, dt:7225.15s, Cycle: 1486 +well_1Control: BHP (at the specified reference elevation): 51197091.24305616 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51198977.811635986 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00466884 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000731726 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.46322e+07s, dt:14450.3s, Cycle: 1487 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 7.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 6.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 6.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 6.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 5.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 9.40e-12 ) ; ( R ) = ( 5.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 8.31e-12 ) ; ( R ) = ( 4.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 7.35e-12 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 4.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 5.00e-12 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.37e-05 ) ; ( Rwell ) = ( 4.72e-15 ) ; ( R ) = ( 3.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00934095 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146146 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.46467e+07s, dt:7225.15s, Cycle: 1488 +well_1Control: BHP (at the specified reference elevation): 51202751.53916927 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.86e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 6.06e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.88e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 2.00e-12 ) ; ( R ) = ( 9.89e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000731626 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.46539e+07s, dt:14450.3s, Cycle: 1489 +well_1Control: BHP (at the specified reference elevation): 51204637.76749618 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 1.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 4.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.46e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 7.07e-12 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 5.50e-12 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.40e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 2.48e-16 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.23e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51208413.06681599 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0093389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00146827 +Time: 7.46683e+07s, dt:14450.3s, Cycle: 1490 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.70e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.05e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 5.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.53e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 4.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 9.64e-12 ) ; ( R ) = ( 4.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 8.47e-12 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 7.43e-12 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 9.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 2.61e-05 ) ; ( Rwell ) = ( 3.27e-15 ) ; ( R ) = ( 2.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00933626 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147249 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.46828e+07s, dt:7225.15s, Cycle: 1491 +well_1Control: BHP (at the specified reference elevation): 51212189.71333827 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 4.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 5.30e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51214073.103915155 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00466708 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000737159 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.469e+07s, dt:14450.3s, Cycle: 1492 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 6.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 6.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 8.48e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 1.83e-15 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00933768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00147821 +Time: 7.47045e+07s, dt:14450.3s, Cycle: 1493 +well_1Control: BHP (at the specified reference elevation): 51217849.89968554 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 4.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.00e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 9.99e-12 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 8.74e-12 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 2.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 5.25e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 9.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.17e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 6.74e-16 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00933401 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148149 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.47189e+07s, dt:7225.15s, Cycle: 1494 +well_1Control: BHP (at the specified reference elevation): 51221626.01681429 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 6.12e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.91e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.72e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.40e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.55e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.62e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.39e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.24e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.11e-12 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000741522 +Time: 7.47261e+07s, dt:7225.15s, Cycle: 1495 +well_1Control: BHP (at the specified reference elevation): 51223512.92608075 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.68e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 5.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.94e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.15e-05 ) ; ( Rwell ) = ( 1.90e-15 ) ; ( R ) = ( 2.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742237 +Time: 7.47334e+07s, dt:7225.15s, Cycle: 1496 +well_1Control: BHP (at the specified reference elevation): 51225400.33750154 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.90e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 4.90e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.97e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.45e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 9.77e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000742689 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.47406e+07s, dt:14450.3s, Cycle: 1497 +well_1Control: BHP (at the specified reference elevation): 51227285.60316482 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 1.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 1.97e-11 ) ; ( R ) = ( 4.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 4.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 9.33e-12 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 7.32e-12 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.84e-12 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 5.18e-12 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.54e-05 ) ; ( Rwell ) = ( 1.43e-15 ) ; ( R ) = ( 3.54e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00933414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00148645 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.4755e+07s, dt:7225.15s, Cycle: 1498 +well_1Control: BHP (at the specified reference elevation): 51231059.416434646 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.91e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.24e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.13e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.87e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.53e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.76e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.38e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.23e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.09e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 9.69e-13 ) ; ( R ) = ( 9.82e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466502 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000743514 +Time: 7.47623e+07s, dt:7225.15s, Cycle: 1499 +well_1Control: BHP (at the specified reference elevation): 51232945.92599803 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.80e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.84e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.43e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.02e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.88e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.67e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.40e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.43e-05 ) ; ( Rwell ) = ( 4.78e-16 ) ; ( R ) = ( 2.43e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466606 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744 +Time: 7.47695e+07s, dt:7225.15s, Cycle: 1500 +well_1Control: BHP (at the specified reference elevation): 51234832.844261624 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.92e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 4.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.88e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.00e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.20e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.68e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.36e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.22e-12 ) ; ( R ) = ( 9.67e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046646 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744396 +Time: 7.47767e+07s, dt:7225.15s, Cycle: 1501 +well_1Control: BHP (at the specified reference elevation): 51236719.26292227 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.57e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.59e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.19e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.00e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.78e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 6.42e-16 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000744741 +Time: 7.47839e+07s, dt:7225.15s, Cycle: 1502 +well_1Control: BHP (at the specified reference elevation): 51238605.7788419 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.48e-04 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.58e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.01e-04 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.62e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.19e-04 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.44e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-04 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.82e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 1.13e-12 ) ; ( R ) = ( 9.90e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466426 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745114 +Time: 7.47912e+07s, dt:7225.15s, Cycle: 1503 +well_1Control: BHP (at the specified reference elevation): 51240491.49195341 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 9.87e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 4.56e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.20e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.86e-05 ) ; ( Rwell ) = ( 5.63e-16 ) ; ( R ) = ( 1.86e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074536 +Time: 7.47984e+07s, dt:7225.15s, Cycle: 1504 +well_1Control: BHP (at the specified reference elevation): 51242378.7622159 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.93e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 9.53e-10 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-04 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.45e-04 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 9.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466311 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745443 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.48056e+07s, dt:14450.3s, Cycle: 1505 +well_1Control: BHP (at the specified reference elevation): 51244263.33478413 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 1.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 5.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 5.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 9.29e-12 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 7.04e-12 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 3.22e-15 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00932971 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00149184 +Time: 7.48201e+07s, dt:14450.3s, Cycle: 1506 +well_1Control: BHP (at the specified reference elevation): 51248036.87020391 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 9.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 6.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.64e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 5.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 9.45e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 8.38e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 6.02e-12 ) ; ( R ) = ( 4.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00932732 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00149233 +Time: 7.48345e+07s, dt:14450.3s, Cycle: 1507 +well_1Control: BHP (at the specified reference elevation): 51251808.75726077 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 9.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.42e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.30e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 8.23e-12 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.40e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 9.39e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 8.80e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 8.25e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.59e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.74e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.40e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; +New dt = 7225.152858510613 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 4.94e-04 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-04 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.68e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-04 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.92e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.50e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 4.92e-12 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 4.92e-12 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466314 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00074611 +coupledFlowAndWells: sub-step = 0, accepted dt = 7225.152858510613, remaining dt = 7225.152858510613 +well_1Control: BHP (at the specified reference elevation): 51253694.303504296 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 9.48e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.06e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 5.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 4.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 1.76e-15 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466461 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000746067 +Time: 7.4849e+07s, dt:7225.15s, Cycle: 1508 +well_1Control: BHP (at the specified reference elevation): 51255579.12510727 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 4.95e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.39e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.54e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 9.85e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51257462.62975499 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00466189 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000745923 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.48562e+07s, dt:14450.3s, Cycle: 1509 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 4.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 4.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 1.22e-11 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 4.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 9.31e-12 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 8.23e-12 ) ; ( R ) = ( 4.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 6.43e-12 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.72e-06 ) ; ( Rwell ) = ( 2.88e-16 ) ; ( R ) = ( 2.72e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00932724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00149512 +Time: 7.48706e+07s, dt:14450.3s, Cycle: 1510 +well_1Control: BHP (at the specified reference elevation): 51261232.24210921 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 9.90e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 6.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 4.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 5.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 9.94e-12 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 9.12e-12 ) ; ( R ) = ( 4.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 7.10e-12 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 4.75e-12 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.83e-05 ) ; ( Rwell ) = ( 1.96e-15 ) ; ( R ) = ( 3.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00932396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00149806 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.48851e+07s, dt:7225.15s, Cycle: 1511 +well_1Control: BHP (at the specified reference elevation): 51265002.74386689 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 4.95e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 5.21e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-04 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.21e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.03e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.50e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.58e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.39e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51266886.102597505 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00466098 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000749669 +Time: 7.48923e+07s, dt:7225.15s, Cycle: 1512 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 9.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.37e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 4.69e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.13e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.81e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.18e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.49e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.33e-05 ) ; ( Rwell ) = ( 4.69e-16 ) ; ( R ) = ( 2.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51268771.18293048 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00466265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000750306 +Time: 7.48995e+07s, dt:7225.15s, Cycle: 1513 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 4.95e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.22e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 9.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00075092 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.49068e+07s, dt:14450.3s, Cycle: 1514 +well_1Control: BHP (at the specified reference elevation): 51270655.110232696 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 1.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.95e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 6.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 6.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 6.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 5.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 5.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 8.99e-12 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 8.15e-12 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 4.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.18e-03 ) ; ( Rwell ) = ( 6.37e-12 ) ; ( R ) = ( 4.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.63e-12 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 4.98e-12 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.80e-05 ) ; ( Rwell ) = ( 9.76e-15 ) ; ( R ) = ( 4.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00932301 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00150411 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.49212e+07s, dt:7225.15s, Cycle: 1515 +well_1Control: BHP (at the specified reference elevation): 51274424.39726904 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 4.97e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.28e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.90e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.63e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.56e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-04 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.85e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.64e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.46e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.30e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.16e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-04 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.96e-04 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 1.04e-12 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51276306.098269254 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00465995 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000752437 +Time: 7.49284e+07s, dt:7225.15s, Cycle: 1516 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 9.89e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 5.81e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.15e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 4.56e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.86e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 9.87e-13 ) ; ( R ) = ( 7.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00465877 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00075302 +Time: 7.49357e+07s, dt:7225.15s, Cycle: 1517 +well_1Control: BHP (at the specified reference elevation): 51278189.29994341 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 7.49e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 6.20e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.99e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 4.94e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 4.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.87e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.66e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 1.85e-15 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466117 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000753394 +Time: 7.49429e+07s, dt:7225.15s, Cycle: 1518 +well_1Control: BHP (at the specified reference elevation): 51280074.933594845 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 4.98e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 4.61e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.08e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.70e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-04 ) ; ( Rwell ) = ( 4.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.59e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-04 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.79e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.61e-04 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.99e-04 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.68e-04 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.60e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.65e-04 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.14e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.33e-04 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.02e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 9.12e-13 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00075386 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.49501e+07s, dt:3612.58s, Cycle: 1519 +well_1Control: BHP (at the specified reference elevation): 51281958.70419965 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 4.74e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.61e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.54e-04 ) ; ( Rwell ) = ( 9.08e-13 ) ; ( R ) = ( 3.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51282900.57681082 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00233108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000377062 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.49537e+07s, dt:7225.15s, Cycle: 1520 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.11e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 7.11e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.21e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.78e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.87e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.73e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.34e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.54e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.36e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.32e-04 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.54e-04 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 1.21e-12 ) ; ( R ) = ( 9.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51284783.397446975 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00465902 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000754399 +Time: 7.49609e+07s, dt:7225.15s, Cycle: 1521 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 9.79e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.74e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.10e-05 ) ; ( Rwell ) = ( 7.53e-17 ) ; ( R ) = ( 2.10e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046601 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000754525 +Time: 7.49682e+07s, dt:7225.15s, Cycle: 1522 +well_1Control: BHP (at the specified reference elevation): 51286667.869706064 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 5.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.97e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.96e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.42e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.46e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.29e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.95e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.49e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.24e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.74e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.80e-04 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.55e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51288550.63490338 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00465849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00075471 +Time: 7.49754e+07s, dt:7225.15s, Cycle: 1523 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 9.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 5.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.33e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.02e-12 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.42e-05 ) ; ( Rwell ) = ( 1.18e-15 ) ; ( R ) = ( 1.42e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.07e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51290435.167679295 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00465956 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000754843 +Time: 7.49826e+07s, dt:7225.15s, Cycle: 1524 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 5.00e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 5.68e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.73e-04 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-04 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.44e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.68e-04 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.57e-04 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.99e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.08e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.89e-04 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.44e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.97e-04 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.48e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.39e-04 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.20e-04 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.41e-04 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.62e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.80e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.95e-04 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.63e-12 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00465798 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000755075 +Time: 7.49898e+07s, dt:7225.15s, Cycle: 1525 +well_1Control: BHP (at the specified reference elevation): 51292315.29803486 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.76e-04 ) ; ( Rwell ) = ( 5.77e-09 ) ; ( R ) = ( 9.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.53e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 5.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 5.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.87e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.79e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.22e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.54e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.99e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.38e-05 ) ; ( Rwell ) = ( 8.32e-16 ) ; ( R ) = ( 2.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00465955 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000754979 +Time: 7.49971e+07s, dt:2928.91s, Cycle: 1526 +well_1Control: BHP (at the specified reference elevation): 51294201.05451296 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.03e-04 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 2.03e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-04 ) ; ( Rwell ) = ( 1.01e-12 ) ; ( R ) = ( 2.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51294964.24251239 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00188857 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000306133 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.5e+07s, dt:5857.81s, Cycle: 1527 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 5.17e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00377567 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000612224 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 3.07879e+07, 3.08284e+07, 3.09406e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.82868e+07, 1.84395e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 742.058 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 27.7779, 714.28 } rm^3 +compflowStatistics, reservoir: Phase mass: { 19221.6, 699421 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2700.91, 218073 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 16520.7, 481348 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 21.5117, 14.9451 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 19200.1, 699406 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 19221.6, 0 }, { 2955.44, 696388 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 3.05814e+07, 3.07279e+07, 3.08066e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.80803e+07, 1.83055e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.701 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.701 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221771 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66531.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155240 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221771 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.00709866, 221771 } } kg +well_1Control: BHP (at the specified reference elevation): 51296484.74624556 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics: Max phase CFL number: 10.6544 +compflowStatistics: Max component CFL number: 14.6304 +Time: 7.50059e+07s, dt:11715.6s, Cycle: 1528 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; ( R ) = ( 1.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.63e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-05 ) ; ( Rwell ) = ( 3.45e-15 ) ; ( R ) = ( 3.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00755675 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122434 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.50176e+07s, dt:23431.2s, Cycle: 1529 +well_1Control: BHP (at the specified reference elevation): 51299541.341783926 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 5.71e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.87e-05 ) ; ( Rwell ) = ( 1.14e-15 ) ; ( R ) = ( 3.87e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244839 +Time: 7.5041e+07s, dt:23431.2s, Cycle: 1530 +well_1Control: BHP (at the specified reference elevation): 51305651.58157732 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 6.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.25e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 8.95e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.91e-05 ) ; ( Rwell ) = ( 5.26e-15 ) ; ( R ) = ( 5.91e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245253 +Time: 7.50644e+07s, dt:23431.2s, Cycle: 1531 +well_1Control: BHP (at the specified reference elevation): 51311762.192481205 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 5.61e-11 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.21e-11 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.23e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.92e-04 ) ; ( Rwell ) = ( 8.40e-12 ) ; ( R ) = ( 6.92e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024547 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.50879e+07s, dt:46862.5s, Cycle: 1532 +well_1Control: BHP (at the specified reference elevation): 51317864.66440561 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.77e-09 ) ; ( R ) = ( 3.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.40e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 1.97e-10 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.78e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 5.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.73e-10 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 4.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.53e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 8.61e-11 ) ; ( R ) = ( 9.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.13e-03 ) ; ( Rwell ) = ( 7.57e-11 ) ; ( R ) = ( 9.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.65e-03 ) ; ( Rwell ) = ( 6.66e-11 ) ; ( R ) = ( 8.65e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.94e-03 ) ; ( Rwell ) = ( 5.86e-11 ) ; ( R ) = ( 7.94e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 5.15e-11 ) ; ( R ) = ( 7.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.75e-03 ) ; ( Rwell ) = ( 4.57e-11 ) ; ( R ) = ( 9.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 8.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 6.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-03 ) ; ( Rwell ) = ( 9.55e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 8.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-03 ) ; ( Rwell ) = ( 5.95e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 8.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 7.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-03 ) ; ( Rwell ) = ( 5.58e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 8.39e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 9.79e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.46e-03 ) ; ( Rwell ) = ( 7.81e-12 ) ; ( R ) = ( 7.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 5.23e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 7.87e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 9.18e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 9.84e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.05e-03 ) ; ( Rwell ) = ( 6.87e-12 ) ; ( R ) = ( 7.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-03 ) ; ( Rwell ) = ( 4.90e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-03 ) ; ( Rwell ) = ( 7.37e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 8.61e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-03 ) ; ( Rwell ) = ( 9.22e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 4.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 6.91e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 8.07e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 8.65e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 5.28e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 7.46e-15 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0301909 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00491108 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.51347e+07s, dt:23431.2s, Cycle: 1533 +well_1Control: BHP (at the specified reference elevation): 51330071.87937756 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 5.63e-11 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.19e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 3.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 1.62e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 9.63e-12 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.51e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.45e-05 ) ; ( Rwell ) = ( 3.58e-15 ) ; ( R ) = ( 5.45e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150897 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245399 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.51582e+07s, dt:11715.6s, Cycle: 1534 +well_1Control: BHP (at the specified reference elevation): 51336176.64885509 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 8.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 8.16e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.49e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.76e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 2.47e-15 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754362 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122658 +Time: 7.51699e+07s, dt:11715.6s, Cycle: 1535 +well_1Control: BHP (at the specified reference elevation): 51339229.711555675 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 8.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.82e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.40e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.66e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.32e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.05e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.82e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.14e-05 ) ; ( Rwell ) = ( 2.25e-15 ) ; ( R ) = ( 2.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754297 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122575 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.51816e+07s, dt:5857.81s, Cycle: 1536 +well_1Control: BHP (at the specified reference elevation): 51342282.6859081 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 4.08e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 4.09e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 2.44e-12 ) ; ( R ) = ( 8.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00377175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000612991 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.51874e+07s, dt:11715.6s, Cycle: 1537 +well_1Control: BHP (at the specified reference elevation): 51343806.43980795 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; ( R ) = ( 1.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 8.28e-12 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 6.40e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 5.67e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.91e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.07e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.72e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 5.73e-16 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122423 +Time: 7.51992e+07s, dt:11715.6s, Cycle: 1538 +well_1Control: BHP (at the specified reference elevation): 51346858.547485046 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 8.15e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 5.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.42e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 4.73e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.18e-04 ) ; ( Rwell ) = ( 4.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 7.84e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.08e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.38e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.19e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.15e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.79e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.17e-06 ) ; ( Rwell ) = ( 2.62e-15 ) ; ( R ) = ( 7.17e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754142 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122502 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.52109e+07s, dt:5857.81s, Cycle: 1539 +well_1Control: BHP (at the specified reference elevation): 51349911.608860694 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 4.07e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 9.38e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00377118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000612673 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.52167e+07s, dt:11715.6s, Cycle: 1540 +well_1Control: BHP (at the specified reference elevation): 51351435.056887306 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; ( R ) = ( 1.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 5.95e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.59e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.04e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.16e-12 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 5.62e-15 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122607 +Time: 7.52285e+07s, dt:11715.6s, Cycle: 1541 +well_1Control: BHP (at the specified reference elevation): 51354487.43375067 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 8.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 1.38e-11 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 7.93e-12 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.25e-04 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 6.15e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.85e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.51e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.21e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.69e-06 ) ; ( Rwell ) = ( 1.79e-15 ) ; ( R ) = ( 7.69e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51357540.59697677 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00753986 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122649 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.52402e+07s, dt:5857.81s, Cycle: 1542 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 4.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.76e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-04 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-04 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.98e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 1.94e-12 ) ; ( R ) = ( 9.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00376987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000613339 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.5246e+07s, dt:11715.6s, Cycle: 1543 +well_1Control: BHP (at the specified reference elevation): 51359064.961333126 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; ( R ) = ( 1.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.50e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.42e-05 ) ; ( Rwell ) = ( 3.26e-15 ) ; ( R ) = ( 1.42e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00754021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00122686 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.52577e+07s, dt:23431.2s, Cycle: 1544 +well_1Control: BHP (at the specified reference elevation): 51362117.50161067 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 5.63e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 3.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 3.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 8.94e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 7.87e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.68e-05 ) ; ( Rwell ) = ( 1.48e-14 ) ; ( R ) = ( 6.68e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150756 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0024535 +Time: 7.52812e+07s, dt:23431.2s, Cycle: 1545 +well_1Control: BHP (at the specified reference elevation): 51368222.58864413 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 5.66e-11 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.82e-05 ) ; ( Rwell ) = ( 6.93e-15 ) ; ( R ) = ( 7.82e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.36e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51374326.79315894 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.015073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00245155 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.53046e+07s, dt:46862.5s, Cycle: 1546 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 3.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 7.25e-09 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 4.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 4.55e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.50e-10 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 7.44e-11 ) ; ( R ) = ( 9.52e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 4.22e-11 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.23e-11 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 9.70e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 9.10e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 8.53e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 8.00e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 9.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.18e-03 ) ; ( Rwell ) = ( 7.50e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 9.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 7.04e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 8.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 6.60e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 9.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.31e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 8.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 6.19e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 9.33e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.87e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 7.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-03 ) ; ( Rwell ) = ( 5.80e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 8.74e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.45e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 7.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 5.44e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 8.20e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 9.57e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 9.04e-12 ) ; ( R ) = ( 7.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 5.10e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 7.68e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 8.97e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 9.61e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 7.97e-12 ) ; ( R ) = ( 6.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 4.79e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 7.20e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.89e-03 ) ; ( Rwell ) = ( 8.41e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-03 ) ; ( Rwell ) = ( 9.01e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 4.49e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 6.75e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 7.88e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 8.45e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 23431.24420428276 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 7.21e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.27e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 5.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.14e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 9.50e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 5.07e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 7.63e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.91e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 9.55e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 6.17e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 4.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 7.15e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 8.35e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 8.95e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.46e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 6.71e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.83e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 8.39e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 4.78e-12 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.18e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 6.29e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.34e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.86e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.92e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 5.90e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 6.88e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 7.37e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 2.05e-15 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150705 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244812 +coupledFlowAndWells: sub-step = 0, accepted dt = 23431.24420428276, remaining dt = 23431.24420428276 +well_1Control: BHP (at the specified reference elevation): 51380430.21715729 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.76e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 5.63e-11 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.83e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 2.44e-11 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-04 ) ; ( Rwell ) = ( 9.43e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 1.61e-12 ) ; ( R ) = ( 9.01e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.015066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244647 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.53515e+07s, dt:46862.5s, Cycle: 1547 +well_1Control: BHP (at the specified reference elevation): 51386531.69921425 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.75e-09 ) ; ( R ) = ( 3.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.26e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.12e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 7.05e-11 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.53e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 6.24e-11 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 5.51e-11 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 4.84e-11 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 4.24e-11 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.96e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.01e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 3.73e-11 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.75e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.13e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.92e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.27e-11 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.24e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.13e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 9.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-03 ) ; ( Rwell ) = ( 9.53e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.43e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 9.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 8.93e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.40e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 9.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-03 ) ; ( Rwell ) = ( 8.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.38e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.11e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.90e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 8.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-03 ) ; ( Rwell ) = ( 7.86e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.07e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.38e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 8.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 7.37e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.30e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.13e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 7.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 6.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.55e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 7.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.20e-03 ) ; ( Rwell ) = ( 6.48e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 9.76e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 7.15e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 7.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.67e-05 ) ; ( Rwell ) = ( 1.29e-14 ) ; ( R ) = ( 4.67e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0301308 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00488768 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.53983e+07s, dt:23431.2s, Cycle: 1548 +well_1Control: BHP (at the specified reference elevation): 51398723.57092662 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 5.57e-11 ) ; ( R ) = ( 5.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 3.19e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.66e-05 ) ; ( Rwell ) = ( 4.58e-16 ) ; ( R ) = ( 3.66e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150601 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00244182 +Time: 7.54218e+07s, dt:23431.2s, Cycle: 1549 +well_1Control: BHP (at the specified reference elevation): 51404821.57732413 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.57e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.48e-04 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 4.48e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51410916.086175025 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0150552 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243856 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.54452e+07s, dt:46862.5s, Cycle: 1550 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 3.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 3.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 5.37e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.96e-10 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.73e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.72e-10 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 4.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 4.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.33e-10 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.17e-10 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.70e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.03e-10 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.22e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.59e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 9.04e-11 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.67e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.13e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 7.95e-11 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 6.99e-11 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.94e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 6.13e-11 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.39e-11 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 4.78e-11 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 4.21e-11 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.70e-11 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 3.26e-11 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 9.48e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 6.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; +New dt = 23431.24420428276 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.22e-03 ) ; ( Rwell ) = ( 5.60e-11 ) ; ( R ) = ( 6.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.31e-03 ) ; ( Rwell ) = ( 4.28e-11 ) ; ( R ) = ( 6.31e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 3.79e-11 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.08e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.56e-05 ) ; ( Rwell ) = ( 2.97e-16 ) ; ( R ) = ( 6.56e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.015055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243353 +coupledFlowAndWells: sub-step = 0, accepted dt = 23431.24420428276, remaining dt = 23431.24420428276 +well_1Control: BHP (at the specified reference elevation): 51417012.4040411 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 5.60e-11 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.81e-03 ) ; ( Rwell ) = ( 3.20e-11 ) ; ( R ) = ( 3.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 8.91e-12 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 7.86e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.31e-05 ) ; ( Rwell ) = ( 1.02e-15 ) ; ( R ) = ( 4.31e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00242709 +Time: 7.54921e+07s, dt:23431.2s, Cycle: 1551 +well_1Control: BHP (at the specified reference elevation): 51423108.44583368 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.60e-03 ) ; ( Rwell ) = ( 5.64e-11 ) ; ( R ) = ( 4.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 3.21e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.76e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.43e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.16e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 9.72e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 8.54e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.60e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.44e-05 ) ; ( Rwell ) = ( 4.44e-15 ) ; ( R ) = ( 5.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.015049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00241933 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.55155e+07s, dt:11715.6s, Cycle: 1552 +well_1Control: BHP (at the specified reference elevation): 51429203.99247452 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 8.07e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.97e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 6.82e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 6.00e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 4.39e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.03e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.70e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.38e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.30e-05 ) ; ( Rwell ) = ( 2.40e-16 ) ; ( R ) = ( 1.30e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0075233 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120745 +Time: 7.55272e+07s, dt:11715.6s, Cycle: 1553 +well_1Control: BHP (at the specified reference elevation): 51432252.41122508 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 8.06e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.05e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 9.66e-12 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 8.52e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 7.51e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.05e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 5.36e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.76e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.21e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.10e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.43e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 1.97e-15 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.03e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51435300.785946175 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00752263 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120528 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.55389e+07s, dt:5857.81s, Cycle: 1554 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.02e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 4.02e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.58e-04 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 5.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00376091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000603337 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.55448e+07s, dt:11715.6s, Cycle: 1555 +well_1Control: BHP (at the specified reference elevation): 51436823.52277817 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 1.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 5.01e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 9.89e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 4.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.80e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.05e-05 ) ; ( Rwell ) = ( 3.90e-15 ) ; ( R ) = ( 2.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00752355 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120827 +Time: 7.55565e+07s, dt:11715.6s, Cycle: 1556 +well_1Control: BHP (at the specified reference elevation): 51439871.0485029 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 8.03e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.16e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.62e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.25e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.55e-12 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.26e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.76e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 2.01e-15 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00752102 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120981 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.55682e+07s, dt:5857.81s, Cycle: 1557 +well_1Control: BHP (at the specified reference elevation): 51442919.388113044 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.01e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 4.01e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.51e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.10e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.84e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-04 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.31e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 3.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-04 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.37e-04 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.17e-04 ) ; ( Rwell ) = ( 1.65e-12 ) ; ( R ) = ( 8.17e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00376042 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000605391 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.55741e+07s, dt:11715.6s, Cycle: 1558 +well_1Control: BHP (at the specified reference elevation): 51444441.856990896 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 1.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.99e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.49e-05 ) ; ( Rwell ) = ( 4.28e-15 ) ; ( R ) = ( 2.49e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00752083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121189 +Time: 7.55858e+07s, dt:11715.6s, Cycle: 1559 +well_1Control: BHP (at the specified reference elevation): 51447491.07520497 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 8.03e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 7.95e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 7.03e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 6.19e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 5.46e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 4.81e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 4.25e-12 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.75e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 3.31e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.01e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.41e-05 ) ; ( Rwell ) = ( 3.57e-15 ) ; ( R ) = ( 2.41e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00751938 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121296 +Time: 7.55975e+07s, dt:11715.6s, Cycle: 1560 +well_1Control: BHP (at the specified reference elevation): 51450540.073702455 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.04e-04 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 8.04e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.09e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 4.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 3.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.85e-04 ) ; ( Rwell ) = ( 3.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.53e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.80e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.49e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.19e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.45e-04 ) ; ( Rwell ) = ( 1.76e-12 ) ; ( R ) = ( 9.45e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00751596 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121408 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.56092e+07s, dt:5857.81s, Cycle: 1561 +well_1Control: BHP (at the specified reference elevation): 51453587.38425099 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-04 ) ; ( Rwell ) = ( 5.72e-09 ) ; ( R ) = ( 4.75e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.62e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.10e-04 ) ; ( Rwell ) = ( 2.09e-12 ) ; ( R ) = ( 9.10e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51455105.8804355 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.003758 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000607212 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.56151e+07s, dt:11715.6s, Cycle: 1562 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.70e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.29e-12 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.57e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.28e-12 ) ; ( R ) = ( 1.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.72e-06 ) ; ( Rwell ) = ( 1.08e-15 ) ; ( R ) = ( 9.72e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00752001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00121517 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.56268e+07s, dt:23431.2s, Cycle: 1563 +well_1Control: BHP (at the specified reference elevation): 51458151.595532954 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.57e-11 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 9.73e-12 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 8.56e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 7.55e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 9.59e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 8.99e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.20e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 8.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.60e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.90e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 4.06e-12 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 7.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.60e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 6.95e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.17e-05 ) ; ( Rwell ) = ( 4.90e-17 ) ; ( R ) = ( 4.17e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243206 +Time: 7.56502e+07s, dt:23431.2s, Cycle: 1564 +well_1Control: BHP (at the specified reference elevation): 51464242.07207976 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 1.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 5.59e-11 ) ; ( R ) = ( 5.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 3.18e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 2.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.12e-04 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 9.12e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150264 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00243194 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.56736e+07s, dt:46862.5s, Cycle: 1565 +well_1Control: BHP (at the specified reference elevation): 51470320.97194877 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 3.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.48e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.04e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 5.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.66e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 3.81e-11 ) ; ( R ) = ( 9.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 9.65e-12 ) ; ( R ) = ( 9.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-03 ) ; ( Rwell ) = ( 5.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-03 ) ; ( Rwell ) = ( 8.56e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 9.99e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 8.50e-12 ) ; ( R ) = ( 8.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 5.33e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-03 ) ; ( Rwell ) = ( 8.02e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-03 ) ; ( Rwell ) = ( 9.37e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 1.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.47e-05 ) ; ( Rwell ) = ( 1.04e-14 ) ; ( R ) = ( 1.47e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51482494.93589555 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0300561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00485672 +Time: 7.57205e+07s, dt:46862.5s, Cycle: 1566 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 3.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.35e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.95e-10 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.36e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 5.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.71e-10 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.15e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.31e-03 ) ; ( Rwell ) = ( 4.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 4.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.83e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 4.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.27e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.20e-03 ) ; ( Rwell ) = ( 4.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.86e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.03e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.46e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 9.00e-11 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 7.95e-11 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.74e-03 ) ; ( Rwell ) = ( 6.95e-11 ) ; ( R ) = ( 8.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.28e-04 ) ; ( Rwell ) = ( 4.55e-14 ) ; ( R ) = ( 1.28e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0300426 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00483693 +Time: 7.57674e+07s, dt:46862.5s, Cycle: 1567 +well_1Control: BHP (at the specified reference elevation): 51494667.026972175 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 3.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 4.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.89e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 4.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 1.47e-10 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 4.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-03 ) ; ( Rwell ) = ( 4.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.31e-10 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 4.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.82e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 3.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-03 ) ; ( Rwell ) = ( 3.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 8.88e-11 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.49e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.74e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 7.87e-11 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 6.92e-11 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.76e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.59e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 6.08e-11 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.96e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.50e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.33e-11 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.90e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 4.69e-11 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.23e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.15e-11 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.51e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.65e-11 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.79e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.21e-11 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.97e-03 ) ; ( Rwell ) = ( 1.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.72e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.60e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 2.80e-11 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 7.00e-05 ) ; ( Rwell ) = ( 8.36e-15 ) ; ( R ) = ( 7.00e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0300319 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00480638 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.58142e+07s, dt:23431.2s, Cycle: 1568 +well_1Control: BHP (at the specified reference elevation): 51506836.666650794 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 1.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.20e-03 ) ; ( Rwell ) = ( 3.12e-11 ) ; ( R ) = ( 4.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 3.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.42e-11 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.99e-03 ) ; ( Rwell ) = ( 2.12e-11 ) ; ( R ) = ( 3.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.39e-05 ) ; ( Rwell ) = ( 1.16e-14 ) ; ( R ) = ( 2.39e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.002401 +Time: 7.58377e+07s, dt:23431.2s, Cycle: 1569 +well_1Control: BHP (at the specified reference elevation): 51512923.27307747 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 5.48e-11 ) ; ( R ) = ( 5.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.02e-03 ) ; ( Rwell ) = ( 3.09e-11 ) ; ( R ) = ( 4.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.78e-03 ) ; ( Rwell ) = ( 2.72e-11 ) ; ( R ) = ( 3.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 2.39e-11 ) ; ( R ) = ( 3.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 3.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.64e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 9.89e-12 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 8.71e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.98e-04 ) ; ( Rwell ) = ( 7.57e-12 ) ; ( R ) = ( 9.98e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240104 +Time: 7.58611e+07s, dt:23431.2s, Cycle: 1570 +well_1Control: BHP (at the specified reference elevation): 51518994.878859654 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 5.50e-11 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.05e-11 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.38e-05 ) ; ( Rwell ) = ( 1.45e-15 ) ; ( R ) = ( 3.38e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0150079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240776 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.58845e+07s, dt:46862.5s, Cycle: 1571 +well_1Control: BHP (at the specified reference elevation): 51525077.936979875 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 3.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.21e-10 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.67e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.98e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.47e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.77e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 1.29e-10 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.88e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.14e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.01e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 8.86e-11 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.54e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.91e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 7.79e-11 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 6.87e-11 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.36e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 9.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 7.78e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-03 ) ; ( Rwell ) = ( 7.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.42e-03 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 8.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 6.84e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 7.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 6.41e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 9.65e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 7.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 6.01e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 9.05e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 9.13e-12 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-03 ) ; ( Rwell ) = ( 5.64e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 8.49e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 9.91e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 6.80e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 6.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 5.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 7.96e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 9.29e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 9.95e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 5.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 4.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 7.46e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 8.71e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 9.33e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 6.25e-12 ) ; ( R ) = ( 5.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 6.99e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 8.16e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 8.74e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 5.83e-03 ) ; ( Rwell ) = ( 5.49e-12 ) ; ( R ) = ( 5.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 4.36e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 6.55e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 7.65e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 8.20e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 23431.24420428276 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.51e-11 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 6.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51531155.357245 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0149999 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00241389 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +coupledFlowAndWells: sub-step = 0, accepted dt = 23431.24420428276, remaining dt = 23431.24420428276 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 5.50e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 9.85e-12 ) ; ( R ) = ( 3.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 8.71e-12 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 7.68e-12 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 6.77e-12 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 9.53e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 8.94e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 5.31e-12 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 8.38e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.41e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.38e-05 ) ; ( Rwell ) = ( 5.67e-15 ) ; ( R ) = ( 6.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0149999 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00241861 +Time: 7.59314e+07s, dt:23431.2s, Cycle: 1572 +well_1Control: BHP (at the specified reference elevation): 51537237.72285816 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 1.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.47e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-05 ) ; ( Rwell ) = ( 1.51e-15 ) ; ( R ) = ( 3.09e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.63e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51543320.98806311 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0149959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00242187 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.59548e+07s, dt:45176.8s, Cycle: 1573 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 3.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.04e-10 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 4.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.97e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.56e-10 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.75e-03 ) ; ( Rwell ) = ( 3.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.37e-10 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 4.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-03 ) ; ( Rwell ) = ( 4.10e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.25e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.91e-03 ) ; ( Rwell ) = ( 3.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 9.33e-11 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.25e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 3.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 8.19e-11 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.25e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.36e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.97e-03 ) ; ( Rwell ) = ( 3.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 7.20e-11 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.64e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.28e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 6.34e-11 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.35e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.81e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 5.60e-11 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.16e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.70e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.95e-11 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.81e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 4.36e-11 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.84e-11 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.51e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.25e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.12e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 3.38e-11 ) ; ( R ) = ( 9.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.16e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.31e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 7.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 6.89e-15 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0289064 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00467307 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.6e+07s, dt:22588.4s, Cycle: 1574 +well_1Control: BHP (at the specified reference elevation): 51555045.177882984 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 5.05e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.90e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 2.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 9.17e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 8.07e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.20e-05 ) ; ( Rwell ) = ( 9.32e-15 ) ; ( R ) = ( 5.20e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0023354 +compflowStatistics, reservoir: Pressure (min, average, max): 3.09879e+07, 3.10283e+07, 3.11407e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.84834e+07, 1.86363e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 742.203 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 28.0757, 714.127 } rm^3 +compflowStatistics, reservoir: Phase mass: { 19490.2, 699379 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2735.43, 218150 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 16754.7, 481229 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 21.0242, 15.4478 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 19469.1, 699363 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 19490.2, 0 }, { 2987.52, 696312 } } kg +well_1Control: BHP (at the specified reference elevation): 51560909.20248743 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 3.07817e+07, 3.09279e+07, 3.10066e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.82773e+07, 1.85021e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.746 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.746 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221846 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66553.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155292 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221846 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.0137417, 221846 } } kg +compflowStatistics: Max phase CFL number: 40.9458 +compflowStatistics: Max component CFL number: 56.2228 +Time: 7.60226e+07s, dt:22588.4s, Cycle: 1575 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 5.02e-11 ) ; ( R ) = ( 5.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.91e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.30e-05 ) ; ( Rwell ) = ( 1.80e-15 ) ; ( R ) = ( 5.30e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51566772.87948482 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.014446 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00233263 +Time: 7.60452e+07s, dt:22588.4s, Cycle: 1576 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 5.06e-11 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 3.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.62e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 2.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.38e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 9.28e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 8.59e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 7.60e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.49e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 7.24e-05 ) ; ( Rwell ) = ( 9.67e-15 ) ; ( R ) = ( 7.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144434 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00232943 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.60678e+07s, dt:11294.2s, Cycle: 1577 +well_1Control: BHP (at the specified reference elevation): 51572636.2341716 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.76e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 7.76e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-04 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 8.02e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.79e-04 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 7.11e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.43e-04 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 3.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 6.32e-12 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.31e-04 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 5.47e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.69e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.32e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.68e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.39e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.26e-05 ) ; ( Rwell ) = ( 9.54e-16 ) ; ( R ) = ( 1.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00722058 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00116545 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.60791e+07s, dt:5647.1s, Cycle: 1578 +well_1Control: BHP (at the specified reference elevation): 51575568.06262122 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-04 ) ; ( Rwell ) = ( 5.69e-09 ) ; ( R ) = ( 3.88e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.65e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-04 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.66e-04 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 8.66e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51577033.43739919 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00361025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00058293 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.60847e+07s, dt:11294.2s, Cycle: 1579 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.39e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.47e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.07e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.57e-05 ) ; ( Rwell ) = ( 6.44e-15 ) ; ( R ) = ( 3.57e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00722133 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00116628 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.6096e+07s, dt:22588.4s, Cycle: 1580 +well_1Control: BHP (at the specified reference elevation): 51579963.367027715 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 5.12e-11 ) ; ( R ) = ( 3.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.99e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 3.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 3.33e-15 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00233297 +Time: 7.61186e+07s, dt:22588.4s, Cycle: 1581 +well_1Control: BHP (at the specified reference elevation): 51585822.40876746 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.68e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 5.10e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.74e-04 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 8.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00233337 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.61412e+07s, dt:45176.8s, Cycle: 1582 +well_1Control: BHP (at the specified reference elevation): 51591667.30888678 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 3.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 2.03e-10 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.74e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.29e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.79e-10 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 1.57e-10 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.62e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 4.65e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.38e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.22e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 4.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.47e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.58e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.07e-10 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.66e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 3.83e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 9.42e-11 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.75e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.05e-03 ) ; ( Rwell ) = ( 3.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 8.29e-11 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.60e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.83e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 7.29e-11 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.73e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 6.41e-11 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 5.63e-11 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 4.95e-11 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 4.36e-11 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.96e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.37e-11 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 9.96e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 8.04e-05 ) ; ( Rwell ) = ( 2.69e-14 ) ; ( R ) = ( 8.04e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.81e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51603376.101322144 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0288649 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00465493 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.61864e+07s, dt:22588.4s, Cycle: 1583 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.70e-03 ) ; ( Rwell ) = ( 5.07e-11 ) ; ( R ) = ( 7.70e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 3.92e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 3.02e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 2.65e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.34e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.87e-05 ) ; ( Rwell ) = ( 1.27e-14 ) ; ( R ) = ( 7.87e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014427 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00232306 +Time: 7.62089e+07s, dt:22588.4s, Cycle: 1584 +well_1Control: BHP (at the specified reference elevation): 51609229.84347136 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.10e-03 ) ; ( Rwell ) = ( 5.10e-11 ) ; ( R ) = ( 4.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 2.55e-11 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.25e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 8.81e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 7.74e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.48e-05 ) ; ( Rwell ) = ( 1.79e-15 ) ; ( R ) = ( 3.48e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144243 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231775 +Time: 7.62315e+07s, dt:22588.4s, Cycle: 1585 +well_1Control: BHP (at the specified reference elevation): 51615082.988245904 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 5.09e-11 ) ; ( R ) = ( 5.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.45e-05 ) ; ( Rwell ) = ( 5.08e-15 ) ; ( R ) = ( 7.45e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144217 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231124 +Time: 7.62541e+07s, dt:22588.4s, Cycle: 1586 +well_1Control: BHP (at the specified reference elevation): 51620935.74408081 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 5.05e-11 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 9.28e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.22e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 8.18e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.24e-05 ) ; ( Rwell ) = ( 4.57e-15 ) ; ( R ) = ( 5.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144191 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0023062 +Time: 7.62767e+07s, dt:22588.4s, Cycle: 1587 +well_1Control: BHP (at the specified reference elevation): 51626787.91458437 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 5.07e-11 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.87e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.88e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.37e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 9.27e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.75e-05 ) ; ( Rwell ) = ( 1.12e-14 ) ; ( R ) = ( 2.75e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.70e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51632640.16934987 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0144164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00230262 +Time: 7.62993e+07s, dt:22588.4s, Cycle: 1588 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.15e-11 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 7.15e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.28e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.88e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.53e-04 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.53e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 9.26e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.89e-04 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 8.68e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.30e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.23e-04 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 1.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 8.14e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.14e-04 ) ; ( Rwell ) = ( 1.53e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.88e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 7.63e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.27e-04 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.21e-04 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.54e-04 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 9.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0144118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229792 +Time: 7.63219e+07s, dt:22588.4s, Cycle: 1589 +well_1Control: BHP (at the specified reference elevation): 51638490.924642764 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.17e-09 ) ; ( R ) = ( 4.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.74e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.43e-03 ) ; ( Rwell ) = ( 3.82e-11 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 3.36e-11 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.83e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 3.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 3.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.81e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.06e-05 ) ; ( Rwell ) = ( 9.18e-15 ) ; ( R ) = ( 5.06e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.34e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51644343.39667329 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0144116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229189 +Time: 7.63445e+07s, dt:22588.4s, Cycle: 1590 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.14e-03 ) ; ( Rwell ) = ( 5.07e-11 ) ; ( R ) = ( 4.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.24e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.97e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.98e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.74e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.86e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 8.70e-10 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.84e-04 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 9.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.47e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51650194.836744905 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.014409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00228831 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.63671e+07s, dt:45176.8s, Cycle: 1591 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 5.65e-09 ) ; ( R ) = ( 3.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 2.02e-10 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.55e-10 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 4.32e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.63e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.37e-10 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 4.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 4.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-03 ) ; ( Rwell ) = ( 4.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.05e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 3.56e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 9.27e-11 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.08e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.68e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 8.16e-11 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.40e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 7.18e-11 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.61e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 6.34e-11 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.84e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.47e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 5.58e-11 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.67e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.07e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.77e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.49e-03 ) ; ( Rwell ) = ( 4.87e-11 ) ; ( R ) = ( 6.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.93e-05 ) ; ( Rwell ) = ( 7.81e-15 ) ; ( R ) = ( 5.93e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.72e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51661884.60675536 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0288107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00460183 +Time: 7.64122e+07s, dt:45176.8s, Cycle: 1592 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 3.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.02e-10 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.55e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.36e-10 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.77e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.05e-10 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.05e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 9.25e-11 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.72e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.53e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.94e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 8.13e-11 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.40e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.17e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.56e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 7.12e-11 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.28e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.42e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.99e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 6.30e-11 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.81e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.40e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 5.53e-11 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.94e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.79e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 4.86e-11 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.09e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 4.32e-11 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.80e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.00e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 9.57e-03 ) ; ( Rwell ) = ( 3.32e-11 ) ; ( R ) = ( 9.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.28e-03 ) ; ( Rwell ) = ( 1.12e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.14e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 2.93e-11 ) ; ( R ) = ( 9.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.04e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.04e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.57e-03 ) ; ( Rwell ) = ( 2.58e-11 ) ; ( R ) = ( 8.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.38e-05 ) ; ( Rwell ) = ( 2.66e-14 ) ; ( R ) = ( 5.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0287992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00462173 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.64574e+07s, dt:22588.4s, Cycle: 1593 +well_1Control: BHP (at the specified reference elevation): 51673572.36559424 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 5.06e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 7.15e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.05e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.73e-04 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.05e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 7.88e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.11e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.24e-04 ) ; ( Rwell ) = ( 6.89e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.75e-04 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.38e-04 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.57e-04 ) ; ( Rwell ) = ( 2.74e-12 ) ; ( R ) = ( 9.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143917 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231291 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.648e+07s, dt:45176.8s, Cycle: 1594 +well_1Control: BHP (at the specified reference elevation): 51679414.58819625 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 3.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 2.01e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.31e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.13e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.26e-03 ) ; ( Rwell ) = ( 2.08e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 8.72e-11 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.32e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 7.68e-11 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.37e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 6.76e-11 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.03e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.90e-11 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.26e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 5.20e-11 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 7.01e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.59e-03 ) ; ( Rwell ) = ( 7.38e-12 ) ; ( R ) = ( 6.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-03 ) ; ( Rwell ) = ( 5.26e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 7.91e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 9.23e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 9.89e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.23e-03 ) ; ( Rwell ) = ( 6.49e-12 ) ; ( R ) = ( 6.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 4.93e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 7.42e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 8.66e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 9.28e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.88e-03 ) ; ( Rwell ) = ( 5.71e-12 ) ; ( R ) = ( 5.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 4.62e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 6.95e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 8.11e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 8.70e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 5.02e-12 ) ; ( R ) = ( 5.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 4.34e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 6.52e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 7.61e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 8.15e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.26e-03 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 5.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 4.06e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 6.11e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 7.13e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 7.64e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 3.89e-12 ) ; ( R ) = ( 4.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 3.81e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 5.73e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 6.69e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 7.16e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.70e-03 ) ; ( Rwell ) = ( 3.42e-12 ) ; ( R ) = ( 4.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-03 ) ; ( Rwell ) = ( 3.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.37e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 6.27e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 6.72e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 3.01e-12 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 3.35e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 5.04e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 5.88e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 6.30e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 2.65e-12 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 3.14e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.72e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 5.51e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.90e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-03 ) ; ( Rwell ) = ( 2.95e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.43e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 5.16e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 5.53e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 3.74e-03 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 3.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-03 ) ; ( Rwell ) = ( 2.76e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 4.15e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.84e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 5.19e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 22588.399337738752 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 5.03e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 4.92e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 3.92e-11 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 3.45e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 2.99e-11 ) ; ( R ) = ( 3.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 2.64e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 2.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.80e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 2.05e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.55e-05 ) ; ( Rwell ) = ( 7.06e-15 ) ; ( R ) = ( 4.55e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143923 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0023139 +coupledFlowAndWells: sub-step = 0, accepted dt = 22588.399337738752, remaining dt = 22588.399337738752 +well_1Control: BHP (at the specified reference elevation): 51685261.08878433 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 5.09e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.80e-05 ) ; ( Rwell ) = ( 5.18e-15 ) ; ( R ) = ( 4.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143889 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231449 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.65252e+07s, dt:45176.8s, Cycle: 1595 +well_1Control: BHP (at the specified reference elevation): 51691107.43120588 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 3.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.01e-10 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 5.28e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.77e-10 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.91e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 4.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.56e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.71e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.37e-10 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.43e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-03 ) ; ( Rwell ) = ( 4.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 4.08e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.34e-03 ) ; ( Rwell ) = ( 3.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 9.31e-11 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 3.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 3.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 8.22e-11 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 3.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 7.24e-11 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.93e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.52e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.29e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 6.37e-11 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.69e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.99e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.64e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.46e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 5.60e-11 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.47e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.97e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.71e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.59e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 4.93e-11 ) ; ( R ) = ( 9.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.67e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.31e-11 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.37e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.85e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.77e-11 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.24e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.05e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 3.32e-11 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.62e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.33e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 7.66e-03 ) ; ( Rwell ) = ( 2.94e-11 ) ; ( R ) = ( 7.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.67e-04 ) ; ( Rwell ) = ( 5.58e-15 ) ; ( R ) = ( 1.67e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.028771 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00462456 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.65704e+07s, dt:22588.4s, Cycle: 1596 +well_1Control: BHP (at the specified reference elevation): 51702793.48568755 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 3.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.71e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 3.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 8.43e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.46e-11 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 9.99e-12 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 8.78e-12 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.96e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.97e-05 ) ; ( Rwell ) = ( 4.90e-15 ) ; ( R ) = ( 5.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51708639.06308961 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143807 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00231022 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.65929e+07s, dt:11294.2s, Cycle: 1597 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 7.70e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-04 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.74e-04 ) ; ( Rwell ) = ( 4.93e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.32e-04 ) ; ( Rwell ) = ( 4.62e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.12e-04 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 4.33e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.16e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 4.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.95e-04 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 3.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 6.10e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.90e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.79e-04 ) ; ( Rwell ) = ( 3.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 5.45e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.83e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.67e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.57e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 3.78e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.47e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.38e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.96e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.12e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.33e-12 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.07e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.85e-05 ) ; ( Rwell ) = ( 2.07e-15 ) ; ( R ) = ( 1.85e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00718921 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115437 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.66042e+07s, dt:5647.1s, Cycle: 1598 +well_1Control: BHP (at the specified reference elevation): 51711562.53499213 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-04 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 3.85e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 2.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 4.23e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.10e-12 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 3.17e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 3.96e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.87e-12 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-04 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 2.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 9.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00359472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000576937 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.66099e+07s, dt:11294.2s, Cycle: 1599 +well_1Control: BHP (at the specified reference elevation): 51713023.19331344 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 1.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 4.23e-12 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 4.24e-12 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.20e-05 ) ; ( Rwell ) = ( 2.52e-15 ) ; ( R ) = ( 1.20e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00718959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00115275 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.66212e+07s, dt:22588.4s, Cycle: 1600 +well_1Control: BHP (at the specified reference elevation): 51715944.97295737 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.63e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 5.03e-11 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 4.22e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.88e-03 ) ; ( Rwell ) = ( 2.83e-11 ) ; ( R ) = ( 3.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.71e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.48e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.61e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.94e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.52e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.36e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 7.78e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.65e-05 ) ; ( Rwell ) = ( 5.84e-15 ) ; ( R ) = ( 2.65e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014375 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229935 +Time: 7.66438e+07s, dt:22588.4s, Cycle: 1601 +well_1Control: BHP (at the specified reference elevation): 51721786.361432284 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 5.00e-11 ) ; ( R ) = ( 5.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 1.93e-11 ) ; ( R ) = ( 3.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.06e-03 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 3.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 9.12e-12 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.59e-05 ) ; ( Rwell ) = ( 1.65e-15 ) ; ( R ) = ( 4.59e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.014372 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229838 +Time: 7.66664e+07s, dt:22588.4s, Cycle: 1602 +well_1Control: BHP (at the specified reference elevation): 51727628.2036114 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 5.02e-11 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 3.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.28e-03 ) ; ( Rwell ) = ( 2.50e-11 ) ; ( R ) = ( 3.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.24e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 3.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 8.89e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 6.95e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.89e-05 ) ; ( Rwell ) = ( 5.62e-15 ) ; ( R ) = ( 5.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51733469.568633094 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.014369 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229617 +Time: 7.66889e+07s, dt:22588.4s, Cycle: 1603 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.62e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 5.04e-11 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 2.84e-11 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 3.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.67e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 9.05e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.06e-05 ) ; ( Rwell ) = ( 1.07e-15 ) ; ( R ) = ( 5.06e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.97e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51739309.87159113 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143662 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229384 +Time: 7.67115e+07s, dt:22588.4s, Cycle: 1604 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 5.03e-11 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 8.90e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.83e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.84e-05 ) ; ( Rwell ) = ( 1.13e-17 ) ; ( R ) = ( 3.84e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143634 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229038 +Time: 7.67341e+07s, dt:22588.4s, Cycle: 1605 +well_1Control: BHP (at the specified reference elevation): 51745150.31958218 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 5.03e-11 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 8.10e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.83e-05 ) ; ( Rwell ) = ( 6.97e-15 ) ; ( R ) = ( 4.83e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.10e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51750990.98118749 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143606 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0022903 +Time: 7.67567e+07s, dt:22588.4s, Cycle: 1606 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.07e-03 ) ; ( Rwell ) = ( 5.09e-11 ) ; ( R ) = ( 4.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.70e-03 ) ; ( Rwell ) = ( 2.86e-11 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 2.22e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 9.09e-12 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.01e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 6.23e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.56e-05 ) ; ( Rwell ) = ( 4.51e-15 ) ; ( R ) = ( 5.56e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.67e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51756831.82884131 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143579 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229503 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.67793e+07s, dt:11294.2s, Cycle: 1607 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 7.63e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 7.00e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.16e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 3.95e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 6.16e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.76e-04 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.42e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.38e-04 ) ; ( Rwell ) = ( 3.47e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.90e-04 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.72e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 2.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.49e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.09e-12 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.73e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.42e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.21e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.99e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.77e-12 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 9.69e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 1.58e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 1.28e-15 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00717776 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114826 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.67906e+07s, dt:5647.1s, Cycle: 1608 +well_1Control: BHP (at the specified reference elevation): 51759752.61181774 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.82e-04 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 3.82e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.26e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-04 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.86e-04 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 1.84e-12 ) ; ( R ) = ( 8.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00358872 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000574308 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.67962e+07s, dt:11294.2s, Cycle: 1609 +well_1Control: BHP (at the specified reference elevation): 51761211.243147686 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.60e-09 ) ; ( R ) = ( 1.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.40e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 2.20e-15 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0071783 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114921 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.68075e+07s, dt:22588.4s, Cycle: 1610 +well_1Control: BHP (at the specified reference elevation): 51764131.34296356 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 5.06e-11 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.21e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 2.87e-11 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.70e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 2.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 1.76e-11 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 3.05e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 9.28e-12 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 7.24e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.64e-05 ) ; ( Rwell ) = ( 5.78e-15 ) ; ( R ) = ( 5.64e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.89e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51769970.830554396 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229966 +Time: 7.68301e+07s, dt:22588.4s, Cycle: 1611 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-03 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 5.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 2.83e-11 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 3.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.58e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 4.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.70e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.40e-05 ) ; ( Rwell ) = ( 1.54e-15 ) ; ( R ) = ( 3.40e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51775809.74487691 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0143493 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229956 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.68527e+07s, dt:45176.8s, Cycle: 1612 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 3.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.98e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.90e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 4.91e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.52e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.06e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-03 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 4.60e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.52e-03 ) ; ( Rwell ) = ( 4.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 4.31e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.18e-10 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-03 ) ; ( Rwell ) = ( 4.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.04e-10 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.76e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.22e-03 ) ; ( Rwell ) = ( 3.79e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 9.13e-11 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.46e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 3.55e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 8.00e-11 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.78e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.10e-03 ) ; ( Rwell ) = ( 6.13e-11 ) ; ( R ) = ( 9.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-04 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.59e-03 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 8.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-03 ) ; ( Rwell ) = ( 7.65e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 1.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.27e-03 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 7.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 7.17e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.08e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.26e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 6.72e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-03 ) ; ( Rwell ) = ( 6.31e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-03 ) ; ( Rwell ) = ( 9.49e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 1.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.23e-03 ) ; ( Rwell ) = ( 9.33e-12 ) ; ( R ) = ( 6.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 5.91e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 8.90e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 1.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.91e-03 ) ; ( Rwell ) = ( 8.21e-12 ) ; ( R ) = ( 5.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.54e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 8.34e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 9.74e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 1.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 5.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-03 ) ; ( Rwell ) = ( 5.20e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 7.82e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 9.13e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 9.78e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 6.36e-12 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 4.87e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 7.33e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 8.56e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 9.17e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 5.60e-12 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-03 ) ; ( Rwell ) = ( 4.57e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 6.87e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 8.02e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 8.60e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 4.96e-12 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 4.29e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 6.44e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 7.52e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.93e-03 ) ; ( Rwell ) = ( 8.06e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 19 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.37e-12 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 4.02e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-03 ) ; ( Rwell ) = ( 6.04e-10 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-03 ) ; ( Rwell ) = ( 7.05e-10 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-03 ) ; ( Rwell ) = ( 7.56e-10 ) ; + Line search failed to produce reduced residual. Accepting iteration. +New dt = 22588.399337738752 + Attempt: 1, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 5.01e-11 ) ; ( R ) = ( 4.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 2.85e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 3.94e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.77e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 3.46e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.51e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.35e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 9.02e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 1, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.95e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 1, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.64e-05 ) ; ( Rwell ) = ( 4.38e-15 ) ; ( R ) = ( 3.64e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143468 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229775 +coupledFlowAndWells: sub-step = 0, accepted dt = 22588.399337738752, remaining dt = 22588.399337738752 +well_1Control: BHP (at the specified reference elevation): 51781647.67710808 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 5.08e-11 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.20e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.71e-11 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 1.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.18e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 8.97e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.64e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 6.96e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 6.06e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 9.62e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 5.34e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 9.02e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.35e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 8.46e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 5.88e-05 ) ; ( Rwell ) = ( 5.59e-15 ) ; ( R ) = ( 5.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143444 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00229474 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.68979e+07s, dt:11294.2s, Cycle: 1613 +well_1Control: BHP (at the specified reference elevation): 51787482.098503575 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 7.66e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.91e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 8.93e-12 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.05e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 7.57e-12 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.94e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.83e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 6.68e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.78e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 6.09e-12 ) ; ( R ) = ( 2.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.49e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 5.37e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.77e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.22e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.74e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.26e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.81e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 9.90e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 1.61e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.19e-05 ) ; ( Rwell ) = ( 3.23e-15 ) ; ( R ) = ( 1.19e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.007171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114713 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.69092e+07s, dt:5647.1s, Cycle: 1614 +well_1Control: BHP (at the specified reference elevation): 51790399.9935124 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 3.83e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.70e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 1.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.06e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-04 ) ; ( Rwell ) = ( 3.15e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 3.69e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.58e-04 ) ; ( Rwell ) = ( 1.56e-12 ) ; ( R ) = ( 9.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00358537 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000573511 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.69148e+07s, dt:11294.2s, Cycle: 1615 +well_1Control: BHP (at the specified reference elevation): 51791857.19268496 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.16e-03 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 3.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.32e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.39e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.62e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 1.31e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.59e-12 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.23e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.21e-06 ) ; ( Rwell ) = ( 5.88e-16 ) ; ( R ) = ( 6.21e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51794775.10864722 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00717053 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114669 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.69261e+07s, dt:22588.4s, Cycle: 1616 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 5.02e-11 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 2.89e-11 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 2.54e-11 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 8.17e-12 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.03e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 1.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 6.38e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 9.64e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.45e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.64e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.34e-05 ) ; ( Rwell ) = ( 6.31e-16 ) ; ( R ) = ( 5.34e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0022915 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.69487e+07s, dt:11294.2s, Cycle: 1617 +well_1Control: BHP (at the specified reference elevation): 51800609.35222244 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 7.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.36e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 1.01e-11 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.28e-04 ) ; ( Rwell ) = ( 4.59e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.94e-12 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.28e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 7.90e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.19e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 6.98e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.03e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.31e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.70e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 4.15e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 3.94e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.50e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.57e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.47e-12 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.13e-05 ) ; ( Rwell ) = ( 3.18e-15 ) ; ( R ) = ( 1.13e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00716783 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114521 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.696e+07s, dt:5647.1s, Cycle: 1618 +well_1Control: BHP (at the specified reference elevation): 51803526.55803615 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 3.83e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.52e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.08e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 1.98e-12 ) ; ( R ) = ( 6.93e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00358388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000572468 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.69657e+07s, dt:11294.2s, Cycle: 1619 +well_1Control: BHP (at the specified reference elevation): 51804983.64277111 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 1.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.31e-11 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-03 ) ; ( Rwell ) = ( 7.50e-12 ) ; ( R ) = ( 3.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 6.63e-12 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.09e-03 ) ; ( Rwell ) = ( 5.70e-12 ) ; ( R ) = ( 3.09e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.03e-12 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 4.44e-12 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 3.92e-12 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 2.71e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 2.40e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.90e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 1.69e-17 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0071688 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114415 +Time: 7.69769e+07s, dt:11294.2s, Cycle: 1620 +well_1Control: BHP (at the specified reference elevation): 51807899.081224695 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.65e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 7.65e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-03 ) ; ( Rwell ) = ( 9.43e-12 ) ; ( R ) = ( 3.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-03 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 2.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.26e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 7.29e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.87e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.56e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 6.44e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 5.66e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 4.92e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 4.03e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.56e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.77e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.45e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 7.88e-16 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51810815.87826271 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00716615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00114333 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.69882e+07s, dt:5647.1s, Cycle: 1621 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.82e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 3.82e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 3.46e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.87e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.12e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.20e-04 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.89e-12 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 1.69e-12 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.09e-04 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-04 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-04 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 1.51e-12 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00358296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000571535 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.69939e+07s, dt:6110.43s, Cycle: 1622 +well_1Control: BHP (at the specified reference elevation): 51812273.319680616 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 1.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.85e-12 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51813848.30816083 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00387561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000617918 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.7e+07s, dt:12220.9s, Cycle: 1623 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 1.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 9.01e-12 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 7.99e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 7.09e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 1.83e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.75e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 3.21e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.30e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.59e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 4.97e-12 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 4.27e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.72e-03 ) ; ( Rwell ) = ( 3.84e-12 ) ; ( R ) = ( 1.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.99e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 2.52e-16 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.73e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51817003.30880779 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00775582 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00123489 +compflowStatistics, reservoir: Pressure (min, average, max): 3.11821e+07, 3.12226e+07, 3.13351e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.86797e+07, 1.88327e+07 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 742.344 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 28.3645, 713.98 } rm^3 +compflowStatistics, reservoir: Phase mass: { 19751.2, 699338 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 2768.63, 218225 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 16982.5, 481113 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 21.7195, 16.0908 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 19729.4, 699322 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 19751.2, 0 }, { 3019.13, 696239 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 3.09764e+07, 3.11223e+07, 3.12008e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.8474e+07, 1.86984e+07 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 226.789 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 226.789 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 221919 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 66575.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 155344 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 221919 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.0251255, 221919 } } kg +compflowStatistics: Max phase CFL number: 22.081 +compflowStatistics: Max component CFL number: 30.3178 +Time: 7.70122e+07s, dt:12220.9s, Cycle: 1624 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 8.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.81e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 8.67e-12 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.15e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 7.67e-12 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 6.78e-12 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 6.01e-12 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 4.47e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.71e-12 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.28e-12 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 2.91e-12 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.34e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 7.01e-06 ) ; ( Rwell ) = ( 3.17e-15 ) ; ( R ) = ( 7.01e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775189 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00123667 +Time: 7.70244e+07s, dt:12220.9s, Cycle: 1625 +well_1Control: BHP (at the specified reference elevation): 51820159.50537354 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 8.25e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 8.57e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.77e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 7.56e-12 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.61e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.19e-03 ) ; ( Rwell ) = ( 6.67e-12 ) ; ( R ) = ( 2.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 5.89e-12 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 5.15e-12 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.04e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 4.55e-12 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.85e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 3.55e-12 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.88e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 2.78e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.17e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.10e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 1.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.06e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.23e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.21e-05 ) ; ( Rwell ) = ( 1.84e-15 ) ; ( R ) = ( 2.21e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00123821 +Time: 7.70367e+07s, dt:12220.9s, Cycle: 1626 +well_1Control: BHP (at the specified reference elevation): 51823315.48970479 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 8.24e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e-03 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 4.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-03 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.07e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 7.78e-12 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.53e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.83e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.13e-03 ) ; ( Rwell ) = ( 7.33e-12 ) ; ( R ) = ( 3.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.77e-03 ) ; ( Rwell ) = ( 5.76e-12 ) ; ( R ) = ( 2.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.61e-03 ) ; ( Rwell ) = ( 5.11e-12 ) ; ( R ) = ( 2.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.74e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 4.02e-12 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.18e-12 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 2.62e-12 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 2.52e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.06e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.85e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.98e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 9.90e-10 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.73e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 1.86e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.83e-12 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 5.23e-16 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00123948 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.70489e+07s, dt:6110.43s, Cycle: 1627 +well_1Control: BHP (at the specified reference elevation): 51826471.31735601 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 4.12e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.51e-04 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 8.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0038747 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000620333 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.7055e+07s, dt:12220.9s, Cycle: 1628 +well_1Control: BHP (at the specified reference elevation): 51828047.00417048 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 1.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 2.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 8.42e-12 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 3.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 7.42e-12 ) ; ( R ) = ( 2.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.94e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.43e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.58e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 3.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 3.23e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 1.61e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 2.42e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 2.27e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.98e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.48e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 2.66e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.45e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.28e-05 ) ; ( Rwell ) = ( 4.01e-16 ) ; ( R ) = ( 1.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0077518 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00124288 +Time: 7.70672e+07s, dt:12220.9s, Cycle: 1629 +well_1Control: BHP (at the specified reference elevation): 51831200.956188954 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.26e-04 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 8.26e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.49e-11 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.22e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.66e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.85e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.93e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 9.71e-12 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.89e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.91e-04 ) ; ( Rwell ) = ( 4.29e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.31e-03 ) ; ( Rwell ) = ( 8.77e-12 ) ; ( R ) = ( 2.31e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.81e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 7.72e-12 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.66e-04 ) ; ( Rwell ) = ( 3.77e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.02e-03 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 2.02e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 4.71e-12 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.60e-03 ) ; ( Rwell ) = ( 4.14e-12 ) ; ( R ) = ( 1.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.51e-03 ) ; ( Rwell ) = ( 3.66e-12 ) ; ( R ) = ( 1.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 3.23e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.86e-12 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.69e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 1.97e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.09e-05 ) ; ( Rwell ) = ( 4.11e-15 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00774828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00124497 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.70794e+07s, dt:6110.43s, Cycle: 1630 +well_1Control: BHP (at the specified reference elevation): 51834356.35113734 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 4.13e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 3.81e-12 ) ; ( R ) = ( 9.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000622989 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.70855e+07s, dt:12220.9s, Cycle: 1631 +well_1Control: BHP (at the specified reference elevation): 51835927.700437844 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 5.56e-09 ) ; ( R ) = ( 1.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-03 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 4.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 4.15e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 8.44e-12 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.07e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 3.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.19e-03 ) ; ( Rwell ) = ( 7.45e-12 ) ; ( R ) = ( 3.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.94e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 2.91e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 3.40e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.00e-03 ) ; ( Rwell ) = ( 6.57e-12 ) ; ( R ) = ( 3.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.01e-03 ) ; ( Rwell ) = ( 3.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 3.42e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.83e-03 ) ; ( Rwell ) = ( 5.80e-12 ) ; ( R ) = ( 2.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-03 ) ; ( Rwell ) = ( 1.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.99e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 3.20e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.66e-03 ) ; ( Rwell ) = ( 5.12e-12 ) ; ( R ) = ( 2.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.60e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.80e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 3.00e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-03 ) ; ( Rwell ) = ( 1.50e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.63e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 2.81e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 4.00e-12 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 2.46e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 2.64e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.68e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.69e-05 ) ; ( Rwell ) = ( 1.82e-15 ) ; ( R ) = ( 1.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00775055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00124791 +Time: 7.70978e+07s, dt:12220.9s, Cycle: 1632 +well_1Control: BHP (at the specified reference elevation): 51839084.243331835 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 8.29e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-03 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 2.79e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.10e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 8.45e-12 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 2.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.14e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.34e-04 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 3.93e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 8.04e-12 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 1.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.95e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.26e-04 ) ; ( Rwell ) = ( 3.68e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 7.13e-12 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 1.84e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.76e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.45e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.72e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 2.59e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 3.24e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 5.63e-12 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 1.62e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 2.43e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 3.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.95e-03 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 1.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 1.52e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 2.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.84e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 4.46e-12 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.42e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.13e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.67e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 3.97e-12 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 1.33e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 2.00e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.50e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 3.54e-12 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-03 ) ; ( Rwell ) = ( 1.25e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 1.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.34e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.10e-05 ) ; ( Rwell ) = ( 7.46e-16 ) ; ( R ) = ( 1.10e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00774657 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0012495 +Time: 7.711e+07s, dt:12220.9s, Cycle: 1633 +well_1Control: BHP (at the specified reference elevation): 51842240.00625709 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.31e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 8.31e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 3.69e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.18e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.27e-04 ) ; ( Rwell ) = ( 4.89e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-03 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 3.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.44e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 3.67e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 4.28e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.81e-04 ) ; ( Rwell ) = ( 4.58e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.44e-03 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 3.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 2.29e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.44e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.82e-04 ) ; ( Rwell ) = ( 4.01e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 4.30e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 9.20e-12 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 3.22e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.75e-04 ) ; ( Rwell ) = ( 3.76e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.91e-04 ) ; ( Rwell ) = ( 4.03e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 8.13e-12 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 2.01e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 3.02e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 3.52e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.78e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 1.89e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 2.83e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.08e-03 ) ; ( Rwell ) = ( 3.30e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 3.54e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 6.37e-12 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.77e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 3.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 3.32e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 5.72e-12 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.49e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.90e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 3.11e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 5.07e-12 ) ; ( R ) = ( 1.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 1.55e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.33e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.72e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 2.92e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-03 ) ; ( Rwell ) = ( 1.46e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 2.19e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.55e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.73e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 4.01e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.37e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.05e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.39e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.56e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 3.57e-12 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 1.28e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.92e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.24e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.40e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 3.17e-12 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 1.20e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 1.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.10e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 2.25e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 9.11e-06 ) ; ( Rwell ) = ( 2.57e-16 ) ; ( R ) = ( 9.11e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.90e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 51845395.72620824 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0077455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00125096 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 7.71222e+07s, dt:6110.43s, Cycle: 1634 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 4.16e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 4.31e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-04 ) ; ( Rwell ) = ( 4.19e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.41e-04 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 8.41e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00387287 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.000626016 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.71283e+07s, dt:12220.9s, Cycle: 1635 +well_1Control: BHP (at the specified reference elevation): 51846971.89445619 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-17 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 5.58e-09 ) ; ( R ) = ( 1.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 2.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 4.18e-09 ) ; +Received signal 11: Segmentation fault + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 439 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 450 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 442 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 435 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 449 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 455 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 447 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 509 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 433 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 453 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 441 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 451 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 432 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 454 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 443 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 438 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 436 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 446 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 448 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 437 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 444 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 434 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 440 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 452 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 445 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 166 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 303 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 57 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 267 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 507 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 508 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 511 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 505 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 510 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 504 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 506 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 146 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 156 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 160 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 411 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 154 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 152 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 418 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 159 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 419 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 157 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 421 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 153 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 425 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 164 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 431 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 165 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 417 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 150 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 426 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 148 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 155 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 163 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 423 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 149 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 416 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 151 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 424 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 161 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 414 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 162 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 427 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 144 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 422 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 167 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 410 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 145 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 429 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 158 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 420 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 147 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 409 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 408 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 412 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 413 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 428 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 430 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 415 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 310 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 55 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 288 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 58 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 265 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 292 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 59 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 279 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 297 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 52 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 283 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_init +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 293 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 56 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 273 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 70 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 269 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 295 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 53 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 272 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 311 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 50 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 268 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 305 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 71 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 286 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 299 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 60 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 285 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 307 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 69 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 278 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 309 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 63 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 264 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 289 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 51 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 282 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 301 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 65 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 266 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 290 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 61 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 287 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 306 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 48 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 277 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 302 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 67 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 271 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 5: opal_progress +Frame 6: ompi_request_default_wait_all +Frame 7: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 8: MPI_Allreduce +Frame 9: hypre_BoomerAMGCoarsenPMISHost +Frame 10: hypre_BoomerAMGCoarsenHMIS +Frame 11: hypre_BoomerAMGSetup +Frame 12: hypre_MGRSetup +Frame 13: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 14: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 15: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 16: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 20: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 22: geosx::EventManager::run(geosx::DomainPartition&) +Frame 23: geosx::GeosxState::run() +Frame 24: main +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: MPI_Waitall +Frame 7: hypre_ParCSRCommHandleDestroy +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 308 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 62 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 276 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 291 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 64 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 280 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 304 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 68 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 270 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 300 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 49 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 281 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 296 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 54 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 284 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libmpi.so.20 +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 298 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 66 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 275 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 294 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 274 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 5: opal_progress +Frame 6: ompi_request_default_wait_all +Frame 7: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 8: MPI_Allreduce +Frame 9: hypre_BoomerAMGCoarsenPMISHost +Frame 10: hypre_BoomerAMGCoarsenHMIS +Frame 11: hypre_BoomerAMGSetup +Frame 12: hypre_MGRSetup +Frame 13: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 14: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 15: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 16: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 20: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 22: geosx::EventManager::run(geosx::DomainPartition&) +Frame 23: geosx::GeosxState::run() +Frame 24: main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 39 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 129 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 317 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 339 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 233 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 392 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 177 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 369 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 253 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 198 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 42 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 313 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 346 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 185 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 40 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 331 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 347 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 403 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 174 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 30 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 328 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 341 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 393 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 172 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 36 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 133 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 327 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 353 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 385 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 186 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 24 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 121 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 325 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 343 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 396 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 33 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 124 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 314 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 389 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 181 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 27 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 120 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 321 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 355 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 398 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 173 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 29 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 136 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 322 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 344 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 386 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 184 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 243 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 43 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 125 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 323 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 349 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 402 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 189 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 249 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 34 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 141 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 319 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 337 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 405 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 187 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 245 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 35 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 128 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 324 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 357 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 388 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 178 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 247 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 26 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 127 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 335 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 354 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 401 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 170 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 255 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 31 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 143 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 316 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 336 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 406 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 176 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 258 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 195 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 25 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 132 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 332 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 359 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 220 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 390 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 183 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 252 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 193 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 46 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 140 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 330 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 356 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 228 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 395 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 190 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 371 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 260 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 213 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 37 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 139 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 326 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 348 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 222 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 397 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 180 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 367 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 251 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 207 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 28 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 122 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 318 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 351 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 231 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 399 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 175 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 365 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 256 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 209 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 32 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 130 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 312 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 352 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 239 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 391 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 191 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 381 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 242 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 215 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 38 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 126 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 315 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 345 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 225 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 407 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 179 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 373 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 254 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 199 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 45 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 142 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 333 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 358 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 221 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 394 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 171 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 377 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 250 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 197 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 41 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 137 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 320 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 350 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 235 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 387 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 182 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 372 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 240 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 192 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 44 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 138 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 334 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 338 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 219 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 400 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 169 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 368 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 261 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 196 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 47 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 123 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 329 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 340 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 224 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 384 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 168 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 378 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 244 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 201 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 134 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 342 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 218 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 404 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 188 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 361 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 259 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 204 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 131 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 216 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 363 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 263 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 206 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 135 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 226 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 380 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 248 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 210 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 230 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 370 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 257 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 194 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 223 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 360 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 246 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 208 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 238 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 376 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 262 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 214 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_init +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 5: opal_progress +Frame 6: ompi_request_default_wait_all +Frame 7: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 8: MPI_Allreduce +Frame 9: hypre_BoomerAMGCoarsenPMISHost +Frame 10: hypre_BoomerAMGCoarsenHMIS +Frame 11: hypre_BoomerAMGSetup +Frame 12: hypre_MGRSetup +Frame 13: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 14: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 15: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 16: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 20: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 22: geosx::EventManager::run(geosx::DomainPartition&) +Frame 23: geosx::GeosxState::run() +Frame 24: main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 234 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 362 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 241 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 200 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 236 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 374 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 212 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 232 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 364 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 203 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 227 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 379 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 205 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 217 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 382 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 211 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 237 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 366 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 202 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 229 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 383 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 375 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 21 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_request_default_wait_all +Frame 2: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 3: MPI_Allreduce +Frame 4: hypre_BoomerAMGCoarsenPMISHost +Frame 5: hypre_BoomerAMGCoarsenHMIS +Frame 6: hypre_BoomerAMGSetup +Frame 7: hypre_MGRSetup +Frame 8: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 9: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 10: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 11: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 12: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 16: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventManager::run(geosx::DomainPartition&) +Frame 18: geosx::GeosxState::run() +Frame 19: main +Frame 20: __libc_start_main +Frame 21: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 5: opal_progress +Frame 6: ompi_request_default_wait_all +Frame 7: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 8: MPI_Allreduce +Frame 9: hypre_BoomerAMGCoarsenPMISHost +Frame 10: hypre_BoomerAMGCoarsenHMIS +Frame 11: hypre_BoomerAMGSetup +Frame 12: hypre_MGRSetup +Frame 13: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 14: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 15: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 16: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 20: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 22: geosx::EventManager::run(geosx::DomainPartition&) +Frame 23: geosx::GeosxState::run() +Frame 24: main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_btl_sm_component_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: mca_pml_ob1_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: MPI_Waitall +Frame 6: hypre_ParCSRCommHandleDestroy +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 21 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_request_default_wait_all +Frame 2: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 3: MPI_Allreduce +Frame 4: hypre_BoomerAMGCoarsenPMISHost +Frame 5: hypre_BoomerAMGCoarsenHMIS +Frame 6: hypre_BoomerAMGSetup +Frame 7: hypre_MGRSetup +Frame 8: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 9: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 10: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 11: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 12: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 16: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventManager::run(geosx::DomainPartition&) +Frame 18: geosx::GeosxState::run() +Frame 19: main +Frame 20: __libc_start_main +Frame 21: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 5: opal_progress +Frame 6: ompi_request_default_wait_all +Frame 7: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 8: MPI_Allreduce +Frame 9: hypre_BoomerAMGCoarsenPMISHost +Frame 10: hypre_BoomerAMGCoarsenHMIS +Frame 11: hypre_BoomerAMGSetup +Frame 12: hypre_MGRSetup +Frame 13: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 14: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 15: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 16: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 20: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 22: geosx::EventManager::run(geosx::DomainPartition&) +Frame 23: geosx::GeosxState::run() +Frame 24: main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 498 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 494 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 496 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 490 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 480 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 485 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 497 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 481 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 503 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 501 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 484 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 488 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 489 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 499 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 495 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 486 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 492 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 502 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 491 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 487 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 482 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 500 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 493 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +-------------------------------------------------------------------------- +MPI_ABORT was invoked on rank 483 in communicator MPI_COMM_WORLD +with errorcode 1. + +NOTE: invoking MPI_ABORT causes Open MPI to kill all MPI processes. +You may or may not see output from other processes, depending on +exactly when Open MPI kills them. +-------------------------------------------------------------------------- +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 22 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: opal_progress +Frame 2: ompi_request_default_wait_all +Frame 3: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 4: MPI_Allreduce +Frame 5: hypre_BoomerAMGCoarsenPMISHost +Frame 6: hypre_BoomerAMGCoarsenHMIS +Frame 7: hypre_BoomerAMGSetup +Frame 8: hypre_MGRSetup +Frame 9: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 10: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 11: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 12: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 13: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 17: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventManager::run(geosx::DomainPartition&) +Frame 19: geosx::GeosxState::run() +Frame 20: main +Frame 21: __libc_start_main +Frame 22: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 6: MPI_Allreduce +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/libopen-pal.so.20 +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: ompi_coll_libnbc_progress +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 5: MPI_Allreduce +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: ompi_coll_base_allreduce_intra_recursivedoubling +Frame 7: MPI_Allreduce +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 23 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_vader.so +Frame 2: opal_progress +Frame 3: ompi_request_default_wait_all +Frame 4: MPI_Waitall +Frame 5: hypre_ParCSRCommHandleDestroy +Frame 6: hypre_BoomerAMGCoarsenPMISHost +Frame 7: hypre_BoomerAMGCoarsenHMIS +Frame 8: hypre_BoomerAMGSetup +Frame 9: hypre_MGRSetup +Frame 10: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 11: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 12: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 13: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 14: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 18: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventManager::run(geosx::DomainPartition&) +Frame 20: geosx::GeosxState::run() +Frame 21: main +Frame 22: __libc_start_main +Frame 23: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 1 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: pthread_spin_lock +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: MPI_Waitall +Frame 7: hypre_ParCSRCommHandleDestroy +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: opal_progress +Frame 4: ompi_request_default_wait_all +Frame 5: MPI_Waitall +Frame 6: hypre_ParCSRCommHandleDestroy +Frame 7: hypre_BoomerAMGCoarsenPMISHost +Frame 8: hypre_BoomerAMGCoarsenHMIS +Frame 9: hypre_BoomerAMGSetup +Frame 10: hypre_MGRSetup +Frame 11: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 12: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 13: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 14: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 15: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 19: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventManager::run(geosx::DomainPartition&) +Frame 21: geosx::GeosxState::run() +Frame 22: main +Frame 23: __libc_start_main +Frame 24: /workrd/SCR/GEOSX/install/gcc8/GEOSX-2e19665/bin/geosx +===== + +Received signal 15: Terminated + +** StackTrace of 24 frames ** +Frame 0: /lib64/libc.so.6 +Frame 1: /usr/lib64/libibverbs/libmlx4-rdmav22.so +Frame 2: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 3: /data_local/sw/OpenMPI/RHEL7/2.1.5/gcc/8.3.0/lib/openmpi/mca_btl_openib.so +Frame 4: opal_progress +Frame 5: ompi_request_default_wait_all +Frame 6: MPI_Waitall +Frame 7: hypre_ParCSRCommHandleDestroy +Frame 8: hypre_BoomerAMGCoarsenPMISHost +Frame 9: hypre_BoomerAMGCoarsenHMIS +Frame 10: hypre_BoomerAMGSetup +Frame 11: hypre_MGRSetup +Frame 12: geosx::HyprePreconditioner::setup(geosx::HypreMatrix const&) +Frame 13: geosx::HypreSolver::setup(geosx::HypreMatrix const&) +Frame 14: geosx::SolverBase::solveLinearSystem(geosx::DofManager const&, geosx::HypreMatrix&, geosx::HypreVector&, geosx::HypreVector&) +Frame 15: geosx::SolverBase::solveNonlinearSystem(double const&, double const&, int, geosx::DomainPartition&) +Frame 16: geosx::SolverBase::nonlinearImplicitStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 17: geosx::SolverBase::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 18: geosx::CoupledSolver::solverStep(double const&, double const&, int, geosx::DomainPartition&) +Frame 19: geosx::SolverBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 20: geosx::EventBase::execute(double, double, int, int, double, geosx::DomainPartition&) +Frame 21: geosx::EventManager::run(geosx::DomainPartition&) +Frame 22: geosx::GeosxState::run() +Frame 23: main +Frame 24: __libc_start_main +===== + diff --git a/geos-posp/tests/Data/job_GEOS_935933.out b/geos-posp/tests/Data/job_GEOS_935933.out new file mode 100644 index 00000000..e9a2fb46 --- /dev/null +++ b/geos-posp/tests/Data/job_GEOS_935933.out @@ -0,0 +1,52347 @@ +GEOSX version: 0.2.0 (HEAD, sha1: 2e19665) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, mesh +Adding Mesh: InternalWell, well_1 +Adding Event: PeriodicEvent, time_steps_1_output +Adding Event: PeriodicEvent, time_steps_1_applications +Adding Event: PeriodicEvent, time_steps_2_output +Adding Event: PeriodicEvent, time_steps_2_applications +Adding Event: PeriodicEvent, statistics +Adding Output: VTK, hexdom_well_module_multiphaseWell + TableFunction: totalRateTable +Adding Object CellElementRegion named caprock from ObjectManager::Catalog. +Adding Object CellElementRegion named reservoir from ObjectManager::Catalog. +Adding Object WellElementRegion named well_1region from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: well_1Control_ConstantBHP_table + TableFunction: well_1Control_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table +VTKMesh 'mesh': reading mesh from /work206/workrd/users/l1045328/job_GEOS/maillage_tresfin/TPFA/Wtrue/hexdom_Wtrue.vtu + reading the dataset... + redistributing mesh... +Generating global Ids from VTK mesh + finding neighbor ranks... + done! +VTKMesh 'mesh': generating GEOSX mesh data structure + preprocessing... + writing nodes... + writing cells... +Importing cell block 3_tetrahedra +Importing cell block 1_tetrahedra +Importing cell block 2_tetrahedra +Importing cell block 3_pyramids +Importing cell block 1_pyramids +Importing cell block 2_pyramids +Importing cell block 2_hexahedra +Importing cell block 3_hexahedra +Importing cell block 1_hexahedra + writing surfaces... +Importing surface 2 +Importing surface 3 +Importing surface 1 + building connectivity maps... + done! +Number of nodes: 2558433 + Number of elems: 3021450 + Polygon: 210306 + C3D4: 304106 + C3D5: 67546 + C3D8: 2439492 +Load balancing: min avg max +(element/rank): 4072 5901 6196 +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_hexahedra +mesh/Level0/caprock/1_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_hexahedra/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_pyramids +mesh/Level0/caprock/1_pyramids/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_pyramids/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_tetrahedra +mesh/Level0/caprock/1_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_tetrahedra/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_hexahedra +mesh/Level0/reservoir/2_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_pyramids +mesh/Level0/reservoir/2_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_tetrahedra +mesh/Level0/reservoir/2_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_hexahedra +mesh/Level0/reservoir/3_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_pyramids +mesh/Level0/reservoir/3_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_tetrahedra +mesh/Level0/reservoir/3_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, well_1region, well_1regionUniqueSubRegion +mesh/Level0/well_1region/well_1regionUniqueSubRegion/fluid allocated 1 quadrature points +mesh/Level0/well_1region/well_1regionUniqueSubRegion/relperm allocated 1 quadrature points +mesh/Level0/well_1region/well_1regionUniqueSubRegion/rockPermregion0 allocated 1 quadrature points +mesh: importing field data from mesh dataset +Time: 0s, dt:100s, Cycle: 0 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 1.98e+01 ) ; ( R ) = ( 1.98e+01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 2.72e-02 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 3, 3.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.43e-05 ) ; ( Rwell ) = ( 1.96e-04 ) ; ( R ) = ( 2.03e-04 ) ; + Last LinSolve(iter,res) = ( 2, 9.37e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20808478.071931716 Pa +well_1Control: Total rate: 2.9566996313953764e-05 kg/s; total surface volumetric rate: 1.999999902888433e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999028871647e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681311928377003e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.271357 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 6.58993e-09 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.24939e+07, 1.25e+07, 1.25339e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.734 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0, 728.734 } rm^3 +compflowStatistics, reservoir: Phase mass: { 0, 703284 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 0, 210985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 0, 492299 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 0, 703284 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 0, 0 }, { 0.00409282, 703284 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.24955e+07, 1.25e+07, 1.25003e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.653 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.653 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214877 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64463.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150414 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214877 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22653e-08, 214877 } } kg +compflowStatistics: Max phase CFL number: 0.0519597 +compflowStatistics: Max component CFL number: 0.0519597 +Time: 100s, dt:200s, Cycle: 1 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 2.08e-02 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.47e-04 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-06 ) ; ( Rwell ) = ( 7.16e-07 ) ; ( R ) = ( 1.87e-06 ) ; + Last LinSolve(iter,res) = ( 5, 9.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.103231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0190843 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 300s, dt:388.282s, Cycle: 2 +well_1Control: BHP (at the specified reference elevation): 20714476.736085214 Pa +well_1Control: Total rate: 2.9566997749602517e-05 kg/s; total surface volumetric rate: 2.0000000000000008e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987327e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254386828e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 5.19e-04 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.26e-02 ) ; ( R ) = ( 5.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 3.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.07e-03 ) ; ( Rwell ) = ( 4.18e-03 ) ; ( R ) = ( 6.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 2.19e-04 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 3, 3.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.49072 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.130864 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 688.282s, dt:245.802s, Cycle: 3 +well_1Control: BHP (at the specified reference elevation): 20826550.973639276 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 9.94e-05 ) ; ( R ) = ( 6.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 2.69e-03 ) ; ( R ) = ( 3.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.97e-06 ) ; ( Rwell ) = ( 5.97e-07 ) ; ( R ) = ( 9.98e-06 ) ; + Last LinSolve(iter,res) = ( 3, 3.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.129158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0542434 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 934.085s, dt:289.201s, Cycle: 4 +well_1Control: BHP (at the specified reference elevation): 20733579.979598 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543865323e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 4.17e-04 ) ; ( R ) = ( 5.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 5.42e-04 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-06 ) ; ( Rwell ) = ( 3.46e-06 ) ; ( R ) = ( 4.69e-06 ) ; + Last LinSolve(iter,res) = ( 5, 9.25e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.104284 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0422849 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1223.29s, dt:392.911s, Cycle: 5 +well_1Control: BHP (at the specified reference elevation): 20655909.49594309 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543862569e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.01e-04 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.20e-03 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-06 ) ; ( Rwell ) = ( 1.04e-05 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0704205 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.038437 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1616.2s, dt:561.783s, Cycle: 6 +well_1Control: BHP (at the specified reference elevation): 20598636.7693571 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543859405e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 1.72e-04 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.35e-03 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-06 ) ; ( Rwell ) = ( 1.18e-05 ) ; ( R ) = ( 1.23e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.76e-04 ) ; +well_1Control: BHP (at the specified reference elevation): 20557176.64878977 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385755e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0444629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0368902 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2177.98s, dt:820.519s, Cycle: 7 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 9.39e-05 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 1.32e-03 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.28e-05 ) ; ( Rwell ) = ( 9.44e-06 ) ; ( R ) = ( 3.41e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.119367 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0380867 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2998.5s, dt:1178.8s, Cycle: 8 +well_1Control: BHP (at the specified reference elevation): 20549477.119754776 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855867e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 1.99e-05 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 1.17e-03 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.71e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.38e-03 ) ; ( Rwell ) = ( 3.04e-04 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 6.27e-07 ) ; ( R ) = ( 2.09e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.133385 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0788198 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4177.3s, dt:1087.45s, Cycle: 9 +well_1Control: BHP (at the specified reference elevation): 20552905.11116146 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.61e-06 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-03 ) ; ( Rwell ) = ( 5.30e-04 ) ; ( R ) = ( 3.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.99e-05 ) ; ( Rwell ) = ( 1.46e-06 ) ; ( R ) = ( 9.99e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0353094 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566387 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5264.75s, dt:1246.01s, Cycle: 10 +well_1Control: BHP (at the specified reference elevation): 20534284.914680507 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385608e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.05e-05 ) ; ( R ) = ( 5.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.90e-03 ) ; ( Rwell ) = ( 3.86e-04 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 8.20e-07 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 5, 1.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0513432 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0467461 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6510.76s, dt:1600.45s, Cycle: 11 +well_1Control: BHP (at the specified reference elevation): 20514189.742151648 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385605e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.88e-05 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.42e-03 ) ; ( Rwell ) = ( 3.52e-04 ) ; ( R ) = ( 4.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-04 ) ; ( Rwell ) = ( 2.71e-07 ) ; ( R ) = ( 1.48e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0434833 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0414254 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8111.21s, dt:2198.85s, Cycle: 12 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.22e-05 ) ; ( R ) = ( 4.84e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 20497075.307260547 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855909e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 3.51e-04 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-05 ) ; ( Rwell ) = ( 7.44e-07 ) ; ( R ) = ( 2.19e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0226828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0393207 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 10310.1s, dt:3106.52s, Cycle: 13 +well_1Control: BHP (at the specified reference elevation): 20485609.504076652 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855768e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 6.56e-06 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.51e-04 ) ; ( R ) = ( 3.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.11e-05 ) ; ( Rwell ) = ( 5.66e-07 ) ; ( R ) = ( 9.11e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0639937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688525 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 13416.6s, dt:3140.85s, Cycle: 14 +well_1Control: BHP (at the specified reference elevation): 20489291.053116158 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 7.56e-07 ) ; ( R ) = ( 5.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 2.05e-04 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.64e-04 ) ; ( Rwell ) = ( 4.40e-08 ) ; ( R ) = ( 3.64e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0353405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669947 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 16557.4s, dt:3233.39s, Cycle: 15 +well_1Control: BHP (at the specified reference elevation): 20489277.46521374 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 5.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.32e-04 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.57e-05 ) ; ( Rwell ) = ( 2.66e-08 ) ; ( R ) = ( 5.57e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20480250.264549915 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855705e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.025828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0508055 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 19790.8s, dt:3956.7s, Cycle: 16 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.14e-06 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.16e-04 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 6.47e-08 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20470426.24281543 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855697e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0303491 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.052036 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 23747.5s, dt:4773.35s, Cycle: 17 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.84e-06 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 1.00e-04 ) ; ( R ) = ( 9.91e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.85e-05 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 5.85e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0209667 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0478639 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 28520.9s, dt:6048.5s, Cycle: 18 +well_1Control: BHP (at the specified reference elevation): 20463151.62836411 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855668e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 9.53e-05 ) ; ( R ) = ( 6.68e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 2.28e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.42e-05 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-05 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 3.62e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0389789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630773 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 34569.4s, dt:6475.43s, Cycle: 19 +well_1Control: BHP (at the specified reference elevation): 20466125.54395666 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 5.48e-07 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 6.60e-05 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 1.66e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.66e-05 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-05 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 2.59e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0304837 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651687 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 41044.8s, dt:6787.75s, Cycle: 20 +well_1Control: BHP (at the specified reference elevation): 20468313.27731094 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.66e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 4.62e-05 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-04 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 1.03e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0582083 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 47832.5s, dt:7646.46s, Cycle: 21 +well_1Control: BHP (at the specified reference elevation): 20465354.989451528 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855645e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 4.96e-07 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 3.73e-05 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-05 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 6.65e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0176169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0508036 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 55479s, dt:9357.17s, Cycle: 22 +well_1Control: BHP (at the specified reference elevation): 20459967.929694764 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.268131254385565e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 7.99e-07 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.46e-05 ) ; ( R ) = ( 3.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-05 ) ; ( Rwell ) = ( 9.72e-10 ) ; ( R ) = ( 4.22e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0128171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0468366 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 64836.2s, dt:12005.7s, Cycle: 23 +well_1Control: BHP (at the specified reference elevation): 20457009.484507374 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855641e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.54e-07 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 3.51e-05 ) ; ( R ) = ( 6.24e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 8.54e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 9.11e-06 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 6.54e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.20e-03 ) ; ( Rwell ) = ( 2.34e-06 ) ; ( R ) = ( 8.20e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.42e-05 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 5.42e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0289523 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0700359 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 76841.8s, dt:12001.6s, Cycle: 24 +well_1Control: BHP (at the specified reference elevation): 20460258.97333862 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.04e-07 ) ; ( R ) = ( 5.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.29e-05 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-04 ) ; ( Rwell ) = ( 7.27e-09 ) ; ( R ) = ( 2.58e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.020444 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661604 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 88843.4s, dt:12457.1s, Cycle: 25 +well_1Control: BHP (at the specified reference elevation): 20461616.697491467 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 5.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.62e-05 ) ; ( R ) = ( 4.25e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151325 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0577165 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 101300s, dt:14107.5s, Cycle: 26 +well_1Control: BHP (at the specified reference elevation): 20460599.231439013 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 9.00e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.34e-05 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.59e-05 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 6.59e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0160515 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557254 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 115408s, dt:16327.1s, Cycle: 27 +well_1Control: BHP (at the specified reference elevation): 20458613.04754882 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.60e-07 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.19e-05 ) ; ( R ) = ( 6.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 2.89e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 3.13e-06 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.73e-05 ) ; ( Rwell ) = ( 3.60e-10 ) ; ( R ) = ( 9.73e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20460512.176226795 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0198561 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624234 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 131735s, dt:17596.9s, Cycle: 28 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.30e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 9.45e-06 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.43e-05 ) ; ( Rwell ) = ( 3.50e-10 ) ; ( R ) = ( 5.43e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.02093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629483 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 149332s, dt:18863.7s, Cycle: 29 +well_1Control: BHP (at the specified reference elevation): 20463393.063748553 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 7.41e-06 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 9.89e-10 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.40e-06 ) ; ( Rwell ) = ( 4.53e-13 ) ; ( R ) = ( 3.40e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0155053 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631357 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 168196s, dt:20183.2s, Cycle: 30 +well_1Control: BHP (at the specified reference elevation): 20464361.91834766 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; ( R ) = ( 5.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 5.67e-06 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-04 ) ; ( Rwell ) = ( 2.43e-09 ) ; ( R ) = ( 1.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0142669 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594499 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 188379s, dt:22437.7s, Cycle: 31 +well_1Control: BHP (at the specified reference elevation): 20464728.30281143 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 4.88e-06 ) ; ( R ) = ( 4.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.33e-04 ) ; ( Rwell ) = ( 7.60e-10 ) ; ( R ) = ( 8.33e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0180397 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646836 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 210817s, dt:23634.3s, Cycle: 32 +well_1Control: BHP (at the specified reference elevation): 20466880.70257048 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.85e-06 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 3.62e-10 ) ; ( R ) = ( 6.22e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0183852 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0614682 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 234451s, dt:25724.6s, Cycle: 33 +well_1Control: BHP (at the specified reference elevation): 20469608.964685775 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 3.24e-06 ) ; ( R ) = ( 4.25e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 1.57e-10 ) ; ( R ) = ( 5.49e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0159321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665699 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 260175s, dt:26593.3s, Cycle: 34 +well_1Control: BHP (at the specified reference elevation): 20471721.83135058 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 9.19e-08 ) ; ( R ) = ( 5.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-04 ) ; ( Rwell ) = ( 5.99e-10 ) ; ( R ) = ( 3.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0161292 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.058578 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 286769s, dt:29839.3s, Cycle: 35 +well_1Control: BHP (at the specified reference elevation): 20473775.68841299 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 8.68e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.51e-02 ) ; ( Rwell ) = ( 2.26e-06 ) ; ( R ) = ( 6.51e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 6.07e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.66e-07 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 4.53e-11 ) ; ( R ) = ( 6.31e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20476672.435852136 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0184326 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661851 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 316608s, dt:30964.3s, Cycle: 36 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 1.76e-06 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 7.70e-10 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-06 ) ; ( Rwell ) = ( 4.47e-14 ) ; ( R ) = ( 2.44e-06 ) ; + Last LinSolve(iter,res) = ( 8, 7.93e-04 ) ; +well_1Control: BHP (at the specified reference elevation): 20479760.335859995 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0187822 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644599 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 347572s, dt:32689.1s, Cycle: 37 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.46e-06 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.68e-10 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 7.00e-14 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 7, 1.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20482847.774717353 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0196083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667001 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 380261s, dt:33749.7s, Cycle: 38 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 3.30e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.84e-07 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.59e-04 ) ; ( Rwell ) = ( 1.93e-10 ) ; ( R ) = ( 6.59e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0153488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630954 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 414011s, dt:36125.3s, Cycle: 39 +well_1Control: BHP (at the specified reference elevation): 20485322.209736027 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 8.20e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 9.84e-07 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 2.12e-10 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-06 ) ; ( Rwell ) = ( 1.54e-13 ) ; ( R ) = ( 2.59e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0212751 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654618 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 450136s, dt:37757.2s, Cycle: 40 +well_1Control: BHP (at the specified reference elevation): 20489278.53085132 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.22e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 8.24e-07 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 2.67e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.06e-07 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.16e-05 ) ; ( Rwell ) = ( 5.61e-12 ) ; ( R ) = ( 8.16e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.58e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20493169.447521552 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0210594 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638196 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 487894s, dt:40118.6s, Cycle: 41 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 6.80e-07 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 2.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 1.80e-07 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e-04 ) ; ( Rwell ) = ( 2.64e-11 ) ; ( R ) = ( 2.05e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0179006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659518 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 528012s, dt:41727.4s, Cycle: 42 +well_1Control: BHP (at the specified reference elevation): 20496335.551873878 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 8.80e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 5.50e-07 ) ; ( R ) = ( 6.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.54e-07 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.99e-04 ) ; ( Rwell ) = ( 6.43e-11 ) ; ( R ) = ( 3.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20500370.68567835 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.022455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639001 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 569740s, dt:44301s, Cycle: 43 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 1.87e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.49e-04 ) ; ( Rwell ) = ( 3.12e-12 ) ; ( R ) = ( 4.49e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0225029 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655102 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 614041s, dt:46279.9s, Cycle: 44 +well_1Control: BHP (at the specified reference elevation): 20504824.415006347 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 4.21e-07 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 1.61e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 8.93e-11 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0209871 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649958 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 660321s, dt:48596s, Cycle: 45 +well_1Control: BHP (at the specified reference elevation): 20508848.83475865 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 9.70e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 3.57e-07 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.38e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 9.81e-08 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.37e-04 ) ; ( Rwell ) = ( 6.50e-11 ) ; ( R ) = ( 5.37e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0237653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662269 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 708917s, dt:50407.3s, Cycle: 46 +well_1Control: BHP (at the specified reference elevation): 20513451.48171423 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.47e-07 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 4.06e-10 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-06 ) ; ( Rwell ) = ( 5.15e-13 ) ; ( R ) = ( 1.60e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0231899 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670091 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 759324s, dt:51885.3s, Cycle: 47 +well_1Control: BHP (at the specified reference elevation): 20518107.017944187 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 3.24e-07 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 1.24e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-04 ) ; ( Rwell ) = ( 7.20e-11 ) ; ( R ) = ( 2.34e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0256693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658058 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 811209s, dt:54044.1s, Cycle: 48 +well_1Control: BHP (at the specified reference elevation): 20523254.531999692 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 2.56e-07 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 6.15e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-04 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 2.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0249013 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649869 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 865253s, dt:56753.7s, Cycle: 49 +well_1Control: BHP (at the specified reference elevation): 20528432.953352854 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.86e-07 ) ; ( R ) = ( 5.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 5.53e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 1.14e-10 ) ; ( R ) = ( 6.37e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0235688 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656629 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 922007s, dt:59198.9s, Cycle: 50 +well_1Control: BHP (at the specified reference elevation): 20533289.19930745 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 9.54e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 2.08e-07 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 9.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-04 ) ; ( Rwell ) = ( 1.65e-11 ) ; ( R ) = ( 1.22e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0285862 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668006 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 981206s, dt:18794.2s, Cycle: 51 +well_1Control: BHP (at the specified reference elevation): 20539215.160419308 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 1.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.20e-03 ) ; ( Rwell ) = ( 6.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 4.61e-09 ) ; ( R ) = ( 3.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 4.94e-13 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0111231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0218368 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1e+06s, dt:34720.3s, Cycle: 52 +well_1Control: BHP (at the specified reference elevation): 20541421.435827173 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 3.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-04 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 3.18e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0143731 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0389119 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.25255e+07, 1.25649e+07, 1.2612e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 23748.7, 110573 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.782 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.0790067, 728.703 } rm^3 +compflowStatistics, reservoir: Phase mass: { 21.4398, 703291 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 3.63289, 211010 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 17.8069, 492280 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.0437189, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 21.3961, 703291 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 21.4398, 0 }, { 9.15496, 703281 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.24811e+07, 1.25074e+07, 1.25442e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): -19575, 42446.4 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.655 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.655 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214880 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64464 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150416 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214880 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2266e-08, 214880 } } kg +well_1Control: BHP (at the specified reference elevation): 20544092.546253726 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.646766 +compflowStatistics: Max component CFL number: 22.3641 +Time: 1.03472e+06s, dt:49323.9s, Cycle: 53 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 8.58e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 8.45e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 6.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.57e-04 ) ; ( Rwell ) = ( 2.81e-11 ) ; ( R ) = ( 3.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0216593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0526166 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08404e+06s, dt:59110s, Cycle: 54 +well_1Control: BHP (at the specified reference elevation): 20548435.137384824 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 9.80e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.09e-07 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 7.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 8.35e-09 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.69e-05 ) ; ( Rwell ) = ( 9.18e-12 ) ; ( R ) = ( 2.69e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0271293 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0615739 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14315e+06s, dt:64267.4s, Cycle: 55 +well_1Control: BHP (at the specified reference elevation): 20554354.84510191 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 6.23e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 8.72e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.15e-04 ) ; ( Rwell ) = ( 2.16e-12 ) ; ( R ) = ( 7.15e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.85e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20560549.484623194 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0286004 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683079 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.20742e+06s, dt:65320s, Cycle: 56 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 5.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 5.35e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 8.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0305722 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662935 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27274e+06s, dt:67710.2s, Cycle: 57 +well_1Control: BHP (at the specified reference elevation): 20566940.2890685 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.09e-07 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 8.50e-08 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 7.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0278677 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639451 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34045e+06s, dt:71853.7s, Cycle: 58 +well_1Control: BHP (at the specified reference elevation): 20572817.242967084 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 9.65e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 7.92e-08 ) ; ( R ) = ( 6.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 6.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.68e-04 ) ; ( Rwell ) = ( 4.76e-11 ) ; ( R ) = ( 5.68e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20579461.117066566 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0310165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667926 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41231e+06s, dt:74117.7s, Cycle: 59 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 8.91e-08 ) ; ( R ) = ( 5.91e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 7.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.13e-04 ) ; ( Rwell ) = ( 2.40e-11 ) ; ( R ) = ( 4.13e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0330749 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070589 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.48642e+06s, dt:73704.3s, Cycle: 60 +well_1Control: BHP (at the specified reference elevation): 20586784.58850641 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 5.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 6.70e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 7.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.73e-04 ) ; ( Rwell ) = ( 1.70e-12 ) ; ( R ) = ( 5.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0305353 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659756 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56013e+06s, dt:76641.8s, Cycle: 61 +well_1Control: BHP (at the specified reference elevation): 20593659.198187146 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 6.26e-08 ) ; ( R ) = ( 6.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 6.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-04 ) ; ( Rwell ) = ( 8.84e-12 ) ; ( R ) = ( 2.35e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0325488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664172 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.63677e+06s, dt:79349.3s, Cycle: 62 +well_1Control: BHP (at the specified reference elevation): 20600665.66157096 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 2.52e-11 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.76e-07 ) ; ( Rwell ) = ( 7.03e-15 ) ; ( R ) = ( 6.76e-07 ) ; + Last LinSolve(iter,res) = ( 9, 6.52e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0337122 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662302 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.71612e+06s, dt:82304.3s, Cycle: 63 +well_1Control: BHP (at the specified reference elevation): 20608224.154930796 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 6.73e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; ( R ) = ( 2.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 5.32e-09 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.05e-05 ) ; ( Rwell ) = ( 4.91e-13 ) ; ( R ) = ( 4.05e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.92e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20616487.501722477 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0373973 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686643 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.79842e+06s, dt:83364.7s, Cycle: 64 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 5.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.68e-07 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 1.74e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 3.25e-13 ) ; ( R ) = ( 4.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0340044 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671396 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.88179e+06s, dt:85699.4s, Cycle: 65 +well_1Control: BHP (at the specified reference elevation): 20623811.925545055 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 9.75e-08 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 6.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.79e-04 ) ; ( Rwell ) = ( 4.20e-11 ) ; ( R ) = ( 7.79e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0359055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663176 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.96749e+06s, dt:32513s, Cycle: 66 +well_1Control: BHP (at the specified reference elevation): 20631849.59277162 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 1.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 7.69e-09 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.90e-03 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 9.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-05 ) ; ( Rwell ) = ( 6.01e-13 ) ; ( R ) = ( 2.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0259423 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2e+06s, dt:56018s, Cycle: 67 +well_1Control: BHP (at the specified reference elevation): 20635540.64949458 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 6.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.96e-09 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 1.06e-12 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0239598 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0454369 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.2578e+07, 1.26174e+07, 1.26627e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 74997.1, 159867 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.82 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.15952, 728.66 } rm^3 +compflowStatistics, reservoir: Phase mass: { 43.5416, 703280 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 7.32136, 211031 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 36.2203, 492249 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.144804, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 43.3968, 703280 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 43.5416, 0 }, { 17.2503, 703262 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.25154e+07, 1.25575e+07, 1.25966e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 13038.9, 93648.8 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.666 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.666 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214899 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64469.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150429 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214899 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22679e-08, 214899 } } kg +well_1Control: BHP (at the specified reference elevation): 20640933.296956524 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.32276 +compflowStatistics: Max component CFL number: 35.6819 +Time: 2.05602e+06s, dt:73124.3s, Cycle: 68 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.70e-04 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 9.70e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0298355 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.12914e+06s, dt:82655.9s, Cycle: 69 +well_1Control: BHP (at the specified reference elevation): 20647507.10016119 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 9.97e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.60e-05 ) ; ( Rwell ) = ( 9.99e-12 ) ; ( R ) = ( 6.60e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0352507 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646574 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.2118e+06s, dt:87087s, Cycle: 70 +well_1Control: BHP (at the specified reference elevation): 20655342.993338548 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 6.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.38e-05 ) ; ( Rwell ) = ( 1.50e-12 ) ; ( R ) = ( 2.38e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.035208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064565 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.29889e+06s, dt:91840.9s, Cycle: 71 +well_1Control: BHP (at the specified reference elevation): 20663273.52691695 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 3.61e-11 ) ; ( R ) = ( 7.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0383825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068863 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.39073e+06s, dt:92846.3s, Cycle: 72 +well_1Control: BHP (at the specified reference elevation): 20672008.025953606 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 5.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 6.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-04 ) ; ( Rwell ) = ( 2.75e-11 ) ; ( R ) = ( 1.03e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0395295 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695365 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.48357e+06s, dt:93257.9s, Cycle: 73 +well_1Control: BHP (at the specified reference elevation): 20681017.61990844 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 9.40e-11 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 4.49e-15 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0374132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642089 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.57683e+06s, dt:98701.6s, Cycle: 74 +well_1Control: BHP (at the specified reference elevation): 20689466.665686443 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; ( R ) = ( 6.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 3.19e-11 ) ; ( R ) = ( 5.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0410782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675636 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.67553e+06s, dt:101046s, Cycle: 75 +well_1Control: BHP (at the specified reference elevation): 20698790.61090131 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 6.15e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 8.52e-09 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.85e-04 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 7.85e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0424907 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685819 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.77658e+06s, dt:102430s, Cycle: 76 +well_1Control: BHP (at the specified reference elevation): 20708632.75817603 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 5.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 1.82e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 8.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 9.17e-09 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-04 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.39e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0424329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682591 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.87901e+06s, dt:104157s, Cycle: 77 +well_1Control: BHP (at the specified reference elevation): 20718361.100070417 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 5.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 8.27e-09 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 3.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0416367 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663976 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.98316e+06s, dt:16835.7s, Cycle: 78 +well_1Control: BHP (at the specified reference elevation): 20727940.198272645 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.24e-03 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 9.00e-10 ) ; ( R ) = ( 6.13e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.85e-05 ) ; ( Rwell ) = ( 4.18e-12 ) ; ( R ) = ( 3.85e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00882216 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0109093 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3e+06s, dt:33671.4s, Cycle: 79 +well_1Control: BHP (at the specified reference elevation): 20729808.722065732 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 1.22e-07 ) ; ( R ) = ( 1.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.30e-05 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 6.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0140807 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0222816 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.26271e+07, 1.26665e+07, 1.27107e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 125391, 209041 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.855 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.235641, 728.62 } rm^3 +compflowStatistics, reservoir: Phase mass: { 64.6734, 703269 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 10.7532, 211050 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 53.9202, 492220 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.208007, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 64.4653, 703269 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 64.6734, 0 }, { 25.0253, 703244 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.25609e+07, 1.26064e+07, 1.26458e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 59302.9, 144033 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.677 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.677 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214917 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64475.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150442 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214917 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22699e-08, 214917 } } kg +compflowStatistics: Max phase CFL number: 0.813297 +compflowStatistics: Max component CFL number: 21.2923 +Time: 3.03367e+06s, dt:61721.2s, Cycle: 80 +well_1Control: BHP (at the specified reference elevation): 20732980.8564178 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 3.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 9.54e-09 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.88e-03 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.83e-03 ) ; ( Rwell ) = ( 8.13e-10 ) ; ( R ) = ( 6.83e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.16e-05 ) ; ( Rwell ) = ( 3.43e-12 ) ; ( R ) = ( 3.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0261486 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0395767 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.09539e+06s, dt:86900.2s, Cycle: 81 +well_1Control: BHP (at the specified reference elevation): 20738913.752500482 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 5.33e-09 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.27e-04 ) ; ( Rwell ) = ( 4.29e-12 ) ; ( R ) = ( 2.27e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0355777 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0576902 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.18229e+06s, dt:98441s, Cycle: 82 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; +well_1Control: BHP (at the specified reference elevation): 20747095.232333526 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 6.15e-09 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.57e-04 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 3.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.60e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20755990.607325066 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.039187 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630107 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.28073e+06s, dt:105461s, Cycle: 83 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.96e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 6.86e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.13e-04 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 7.13e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.042479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665691 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.38619e+06s, dt:109023s, Cycle: 84 +well_1Control: BHP (at the specified reference elevation): 20765855.12030088 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 4.35e-12 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0442371 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679485 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.49522e+06s, dt:111196s, Cycle: 85 +well_1Control: BHP (at the specified reference elevation): 20776223.580697447 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.05e-07 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 7.00e-09 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0448139 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685653 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.60641e+06s, dt:112736s, Cycle: 86 +well_1Control: BHP (at the specified reference elevation): 20786676.466470324 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0456057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658665 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.71915e+06s, dt:117356s, Cycle: 87 +well_1Control: BHP (at the specified reference elevation): 20797298.66298972 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 7.14e-09 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.18e-04 ) ; ( Rwell ) = ( 2.06e-12 ) ; ( R ) = ( 6.18e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0462605 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687915 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.83651e+06s, dt:118723s, Cycle: 88 +well_1Control: BHP (at the specified reference elevation): 20808022.678213578 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 2.96e-07 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.86e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 7.21e-09 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.53e-04 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 3.53e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0478642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681994 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.95523e+06s, dt:44770s, Cycle: 89 +well_1Control: BHP (at the specified reference elevation): 20819196.74727977 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 1.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 3.83e-11 ) ; ( R ) = ( 4.00e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20823713.683511652 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0197117 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0264291 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4e+06s, dt:76524.9s, Cycle: 90 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.11e-07 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 9.73e-09 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 6.52e-13 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0306163 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0446647 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.2679e+07, 1.27184e+07, 1.27617e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 175121, 257933 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.893 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.315952, 728.577 } rm^3 +compflowStatistics, reservoir: Phase mass: { 87.2207, 703258 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 14.5312, 211070 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 72.6895, 492188 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.291405, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 86.9293, 703258 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 87.2207, 0 }, { 33.3124, 703224 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.26123e+07, 1.26583e+07, 1.26976e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 108553, 193762 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.688 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.688 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214937 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64481.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150456 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214937 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22719e-08, 214937 } } kg +well_1Control: BHP (at the specified reference elevation): 20830870.08741968 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.84249 +compflowStatistics: Max component CFL number: 48.0657 +Time: 4.07652e+06s, dt:100862s, Cycle: 91 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 5.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 4.93e-09 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.11e-04 ) ; ( Rwell ) = ( 4.26e-12 ) ; ( R ) = ( 3.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0396881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568826 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.17739e+06s, dt:115261s, Cycle: 92 +well_1Control: BHP (at the specified reference elevation): 20840171.19951562 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; ( R ) = ( 6.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.59e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-04 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 1.99e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0452637 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646775 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.29265e+06s, dt:121416s, Cycle: 93 +well_1Control: BHP (at the specified reference elevation): 20850749.038550522 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 5.59e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 6.32e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 1.47e-11 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0477169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666027 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.41406e+06s, dt:125475s, Cycle: 94 +well_1Control: BHP (at the specified reference elevation): 20862007.716807365 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 6.31e-09 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.78e-04 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 9.78e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0502735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701577 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.53954e+06s, dt:125287s, Cycle: 95 +well_1Control: BHP (at the specified reference elevation): 20873820.952525597 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; ( R ) = ( 6.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 5.72e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 6.27e-09 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 9.36e-12 ) ; ( R ) = ( 4.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0489617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670519 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.66483e+06s, dt:128907s, Cycle: 96 +well_1Control: BHP (at the specified reference elevation): 20885364.63493996 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 5.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 6.66e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.02e-04 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 4.02e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0511448 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692526 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.79373e+06s, dt:129831s, Cycle: 97 +well_1Control: BHP (at the specified reference elevation): 20897437.52030408 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.36e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 5.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.24e-04 ) ; ( Rwell ) = ( 2.79e-11 ) ; ( R ) = ( 6.24e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0505748 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661006 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.92356e+06s, dt:76436.5s, Cycle: 98 +well_1Control: BHP (at the specified reference elevation): 20909339.965028737 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 2.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 8.20e-09 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.29e-04 ) ; ( Rwell ) = ( 3.35e-12 ) ; ( R ) = ( 3.29e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311341 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0409532 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5e+06s, dt:105668s, Cycle: 99 +well_1Control: BHP (at the specified reference elevation): 20916595.12603961 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 5.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.12e-05 ) ; ( Rwell ) = ( 1.27e-12 ) ; ( R ) = ( 8.12e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0413108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0541137 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.27293e+07, 1.27687e+07, 1.28113e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 224127, 306222 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.93 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.39376, 728.536 } rm^3 +compflowStatistics, reservoir: Phase mass: { 109.315, 703247 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 18.3397, 211089 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 90.9754, 492158 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.325109, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 108.99, 703247 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 109.315, 0 }, { 41.6469, 703205 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.26632e+07, 1.27088e+07, 1.27479e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 157961, 242768 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.699 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.699 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214956 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64486.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150469 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214956 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22739e-08, 214956 } } kg +well_1Control: BHP (at the specified reference elevation): 20926399.448625777 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.50929 +compflowStatistics: Max component CFL number: 65.9631 +Time: 5.10567e+06s, dt:124505s, Cycle: 100 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 5.32e-09 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.82e-04 ) ; ( Rwell ) = ( 6.55e-12 ) ; ( R ) = ( 3.82e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0483045 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638998 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.23017e+06s, dt:132185s, Cycle: 101 +well_1Control: BHP (at the specified reference elevation): 20937638.83635222 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 9.87e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 5.98e-09 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 5.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20949818.359052096 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0512013 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671789 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.36236e+06s, dt:135835s, Cycle: 102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 7.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 5.57e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 3.34e-11 ) ; ( R ) = ( 4.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0524242 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695215 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.49819e+06s, dt:136457s, Cycle: 103 +well_1Control: BHP (at the specified reference elevation): 20962253.748753764 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 9.99e-08 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 6.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 4.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 5.17e-09 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.03e-04 ) ; ( Rwell ) = ( 3.25e-11 ) ; ( R ) = ( 5.03e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.96e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 20974919.403072134 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.053314 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670739 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.63465e+06s, dt:140368s, Cycle: 104 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.01e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 7.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 4.41e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0539296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681715 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.77502e+06s, dt:142856s, Cycle: 105 +well_1Control: BHP (at the specified reference elevation): 20987788.61005818 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 9.99e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.33e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; ( R ) = ( 8.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 6.01e-09 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.69e-04 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 6.69e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0547365 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0707069 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.91787e+06s, dt:82125.9s, Cycle: 106 +well_1Control: BHP (at the specified reference elevation): 21000669.006313354 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 9.82e-08 ) ; ( R ) = ( 3.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.05e-07 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.46e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-04 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 2.16e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0333529 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0417236 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6e+06s, dt:112393s, Cycle: 107 +well_1Control: BHP (at the specified reference elevation): 21008517.72988698 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 1.22e-12 ) ; ( R ) = ( 3.55e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21018743.466224052 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0429429 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0567831 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.27778e+07, 1.28172e+07, 1.28593e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 272387, 353953 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.965 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.468439, 728.497 } rm^3 +compflowStatistics, reservoir: Phase mass: { 130.755, 703237 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 22.1157, 211108 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 108.639, 492129 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.339588, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 130.415, 703237 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 130.755, 0 }, { 49.9734, 703186 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.27123e+07, 1.27575e+07, 1.27964e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 206851, 291029 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.71 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.71 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214975 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64492.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150482 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214975 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22758e-08, 214975 } } kg +compflowStatistics: Max phase CFL number: 2.63013 +compflowStatistics: Max component CFL number: 69.7596 +Time: 6.11239e+06s, dt:128578s, Cycle: 108 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 9.91e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 4.78e-09 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-04 ) ; ( Rwell ) = ( 2.21e-11 ) ; ( R ) = ( 3.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0490973 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642029 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.24097e+06s, dt:136092s, Cycle: 109 +well_1Control: BHP (at the specified reference elevation): 21030453.708977655 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 9.91e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.23e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 8.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 5.13e-09 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 7.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.051784 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636973 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.37706e+06s, dt:144782s, Cycle: 110 +well_1Control: BHP (at the specified reference elevation): 21042739.181921005 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 9.82e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.91e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; ( R ) = ( 8.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 5.54e-09 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-04 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 2.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0549146 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686399 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.52185e+06s, dt:146682s, Cycle: 111 +well_1Control: BHP (at the specified reference elevation): 21055740.22368343 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 9.76e-08 ) ; ( R ) = ( 5.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.23e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; ( R ) = ( 9.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 5.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 5.71e-09 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 3.33e-11 ) ; ( R ) = ( 4.36e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21069060.159529023 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0554545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715959 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.66853e+06s, dt:144486s, Cycle: 112 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 9.86e-08 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; ( R ) = ( 7.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 5.45e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.34e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.82e-04 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.82e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0544581 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663555 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.81301e+06s, dt:149682s, Cycle: 113 +well_1Control: BHP (at the specified reference elevation): 21082107.008280605 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 9.80e-08 ) ; ( R ) = ( 5.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.67e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 8.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 5.51e-09 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 5.27e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0562391 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068892 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.9627e+06s, dt:37304.2s, Cycle: 114 +well_1Control: BHP (at the specified reference elevation): 21095524.684113815 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 9.72e-08 ) ; ( R ) = ( 1.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-04 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 1.42e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0158444 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0178972 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7e+06s, dt:74048.2s, Cycle: 115 +well_1Control: BHP (at the specified reference elevation): 21099163.567474004 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 1.06e-07 ) ; ( R ) = ( 2.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 5.70e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 1.34e-12 ) ; ( R ) = ( 4.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0282479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0360495 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.28234e+07, 1.28628e+07, 1.29045e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 319851, 400968 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.998 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.538499, 728.46 } rm^3 +compflowStatistics, reservoir: Phase mass: { 151.079, 703228 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 25.836, 211126 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 125.243, 492102 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.447174, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 150.632, 703228 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 151.079, 0 }, { 58.0823, 703169 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.27586e+07, 1.28033e+07, 1.28421e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 255068, 338496 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.72 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.72 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214992 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64497.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150495 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214992 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22776e-08, 214992 } } kg +compflowStatistics: Max phase CFL number: 1.71049 +compflowStatistics: Max component CFL number: 45.7168 +Time: 7.07405e+06s, dt:109432s, Cycle: 116 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 21105955.260072045 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 9.95e-08 ) ; ( R ) = ( 4.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 3.56e-11 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-05 ) ; ( Rwell ) = ( 5.31e-15 ) ; ( R ) = ( 3.12e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.56e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0409977 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0524158 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.18348e+06s, dt:131445s, Cycle: 117 +well_1Control: BHP (at the specified reference elevation): 21115862.518938366 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 9.81e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-03 ) ; ( Rwell ) = ( 3.04e-11 ) ; ( R ) = ( 1.69e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.98e-05 ) ; ( Rwell ) = ( 1.17e-14 ) ; ( R ) = ( 5.98e-05 ) ; + Last LinSolve(iter,res) = ( 7, 1.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0491831 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624105 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.31492e+06s, dt:141686s, Cycle: 118 +well_1Control: BHP (at the specified reference elevation): 21127711.223787338 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 9.76e-08 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 5.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-04 ) ; ( Rwell ) = ( 2.13e-11 ) ; ( R ) = ( 3.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0528984 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667107 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.45661e+06s, dt:146268s, Cycle: 119 +well_1Control: BHP (at the specified reference elevation): 21140343.523536388 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 9.65e-08 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; ( R ) = ( 7.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 1.90e-11 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0544481 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695413 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.60288e+06s, dt:146910s, Cycle: 120 +well_1Control: BHP (at the specified reference elevation): 21153380.33655116 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 9.64e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.22e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 8.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 5.06e-09 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.56e-04 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 3.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0545119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656613 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.74979e+06s, dt:153242s, Cycle: 121 +well_1Control: BHP (at the specified reference elevation): 21166477.558663085 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 9.64e-08 ) ; ( R ) = ( 5.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 4.17e-11 ) ; ( R ) = ( 5.98e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.056661 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682519 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.90303e+06s, dt:96970.8s, Cycle: 122 +well_1Control: BHP (at the specified reference elevation): 21180046.66359138 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 9.57e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 7.15e-09 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-04 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 3.20e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.75e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21189018.083939526 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0373758 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0448023 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8e+06s, dt:127590s, Cycle: 123 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 9.99e-08 ) ; ( R ) = ( 4.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 1.72e-07 ) ; ( R ) = ( 5.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 7.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-04 ) ; ( Rwell ) = ( 7.05e-12 ) ; ( R ) = ( 2.03e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0470002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585956 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.28727e+07, 1.29121e+07, 1.29533e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 366823, 447517 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.034 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.613964, 728.42 } rm^3 +compflowStatistics, reservoir: Phase mass: { 173.199, 703218 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 29.972, 211145 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 143.227, 492073 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.450788, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 172.749, 703218 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 173.199, 0 }, { 67.1125, 703150 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.28086e+07, 1.28529e+07, 1.28914e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 302626, 385468 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.731 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.731 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215011 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64503.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150508 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215011 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22796e-08, 215011 } } kg +well_1Control: BHP (at the specified reference elevation): 21200261.28570158 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.89411 +compflowStatistics: Max component CFL number: 78.3298 +Time: 8.12759e+06s, dt:143136s, Cycle: 124 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 9.51e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.62e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 8.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 4.37e-09 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-04 ) ; ( Rwell ) = ( 3.94e-11 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.55e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21212831.87204936 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0525814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660604 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.27073e+06s, dt:148716s, Cycle: 125 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.48e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.78e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 7.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 4.39e-09 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 5.83e-11 ) ; ( R ) = ( 4.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0544829 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658531 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.41944e+06s, dt:154831s, Cycle: 126 +well_1Control: BHP (at the specified reference elevation): 21226085.855747834 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.62e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 5.33e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.62e-04 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 5.62e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21239755.415342834 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0565322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689474 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.57427e+06s, dt:156398s, Cycle: 127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 9.51e-08 ) ; ( R ) = ( 5.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 7.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.80e-04 ) ; ( Rwell ) = ( 2.59e-11 ) ; ( R ) = ( 3.80e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0569266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708214 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.73067e+06s, dt:155184s, Cycle: 128 +well_1Control: BHP (at the specified reference elevation): 21253543.57241028 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 9.49e-08 ) ; ( R ) = ( 5.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 8.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 4.87e-09 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.73e-04 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 2.73e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0562881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671583 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.88585e+06s, dt:114145s, Cycle: 129 +well_1Control: BHP (at the specified reference elevation): 21267068.056030937 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 9.38e-08 ) ; ( R ) = ( 3.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 4.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.78e-03 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 9.19e-10 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.25e-05 ) ; ( Rwell ) = ( 6.26e-13 ) ; ( R ) = ( 6.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0424539 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0506929 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9e+06s, dt:139863s, Cycle: 130 +well_1Control: BHP (at the specified reference elevation): 21277354.57016623 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 9.69e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 4.11e-09 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.96e-04 ) ; ( Rwell ) = ( 8.80e-12 ) ; ( R ) = ( 6.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0505229 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0614409 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 21289645.783205494 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.29193e+07, 1.29587e+07, 1.29996e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 412895, 493231 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.068 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.684945, 728.383 } rm^3 +compflowStatistics, reservoir: Phase mass: { 194.226, 703210 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 34.0737, 211163 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 160.152, 492047 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.599349, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 193.626, 703210 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 194.226, 0 }, { 76.0163, 703132 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.28559e+07, 1.28996e+07, 1.2938e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 349443, 431541 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.742 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.742 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215029 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64508.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150520 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215029 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22814e-08, 215029 } } kg +compflowStatistics: Max phase CFL number: 3.12504 +compflowStatistics: Max component CFL number: 85.4127 +Time: 9.13986e+06s, dt:152275s, Cycle: 131 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 9.44e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 3.19e-07 ) ; ( R ) = ( 6.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.92e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 4.32e-09 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 2.53e-11 ) ; ( R ) = ( 4.95e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0548619 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068728 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.29214e+06s, dt:154143s, Cycle: 132 +well_1Control: BHP (at the specified reference elevation): 21302900.500230372 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 9.35e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.11e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 8.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 5.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 3.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.07e-04 ) ; ( Rwell ) = ( 2.36e-11 ) ; ( R ) = ( 8.07e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0553664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658608 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.44628e+06s, dt:160469s, Cycle: 133 +well_1Control: BHP (at the specified reference elevation): 21316361.604165427 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 9.38e-08 ) ; ( R ) = ( 5.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 7.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 5.02e-09 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.55e-04 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 4.55e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21330373.01486384 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0574565 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667147 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.60675e+06s, dt:165651s, Cycle: 134 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 9.37e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; ( R ) = ( 7.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 6.06e-11 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0591272 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068631 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.7724e+06s, dt:167840s, Cycle: 135 +well_1Control: BHP (at the specified reference elevation): 21344807.081598204 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 9.35e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.98e-04 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 7.98e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0597374 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694444 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.94024e+06s, dt:59759.2s, Cycle: 136 +well_1Control: BHP (at the specified reference elevation): 21359471.646751493 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 9.36e-08 ) ; ( R ) = ( 1.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 8.14e-11 ) ; ( R ) = ( 2.83e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.022603 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0264182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1e+07s, dt:102164s, Cycle: 137 +well_1Control: BHP (at the specified reference elevation): 21364903.444289166 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 9.74e-08 ) ; ( R ) = ( 3.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 7.19e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 3.46e-11 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 6.48e-16 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.22e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0363067 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0434907 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.29631e+07, 1.30025e+07, 1.30431e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 458429, 538492 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.1 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.751458, 728.348 } rm^3 +compflowStatistics, reservoir: Phase mass: { 214.122, 703202 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 37.9966, 211180 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 176.126, 492022 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.729113, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 213.393, 703202 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 214.122, 0 }, { 84.572, 703116 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.29002e+07, 1.29435e+07, 1.29817e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 395554, 477076 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.752 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.752 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215046 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64513.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150532 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215046 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22831e-08, 215046 } } kg +compflowStatistics: Max phase CFL number: 2.25992 +compflowStatistics: Max component CFL number: 62.0841 +Time: 1.01022e+07s, dt:136669s, Cycle: 138 +well_1Control: BHP (at the specified reference elevation): 21373824.02442013 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 9.34e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.93e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 5.93e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.048483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.058058 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02388e+07s, dt:154207s, Cycle: 139 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 9.25e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 2.89e-07 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 1.67e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 4.26e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21385638.945209354 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-04 ) ; ( Rwell ) = ( 2.37e-11 ) ; ( R ) = ( 2.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.054574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642795 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.0393e+07s, dt:163092s, Cycle: 140 +well_1Control: BHP (at the specified reference elevation): 21398953.618568007 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 9.24e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 7.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.60e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 6.46e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.057551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676239 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.05561e+07s, dt:166868s, Cycle: 141 +well_1Control: BHP (at the specified reference elevation): 21413053.895779304 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 9.24e-08 ) ; ( R ) = ( 5.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.14e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 9.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.18e-04 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 3.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0586435 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673738 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.0723e+07s, dt:171149s, Cycle: 142 +well_1Control: BHP (at the specified reference elevation): 21427156.479779225 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 9.03e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 2.38e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 4.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 6.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 7.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 6.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 6.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 5.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 6.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.35e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 5.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 8.88e-09 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.30e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 5.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 7.91e-09 ) ; ( R ) = ( 1.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.70e-02 ) ; ( Rwell ) = ( 7.11e-09 ) ; ( R ) = ( 9.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 5.97e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.21e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.27e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.30e-02 ) ; ( Rwell ) = ( 5.45e-09 ) ; ( R ) = ( 8.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.94e-04 ) ; ( Rwell ) = ( 1.92e-11 ) ; ( R ) = ( 6.94e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0599033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706967 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.08941e+07s, dt:105851s, Cycle: 143 +well_1Control: BHP (at the specified reference elevation): 21441889.06034112 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 9.19e-08 ) ; ( R ) = ( 3.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 8.81e-09 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-04 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 3.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0383088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0472866 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.1e+07s, dt:135069s, Cycle: 144 +well_1Control: BHP (at the specified reference elevation): 21451250.869193926 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 9.43e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 3.15e-09 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.44e-04 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 5.44e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0471157 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0563868 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.30094e+07, 1.30487e+07, 1.30891e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 503290, 583089 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.133 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.821474, 728.312 } rm^3 +compflowStatistics, reservoir: Phase mass: { 235.272, 703194 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 42.2684, 211198 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 193.004, 491995 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0.864552, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 234.407, 703194 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 235.272, 0 }, { 93.9624, 703098 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.29472e+07, 1.299e+07, 1.3028e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 441070, 521939 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.762 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.762 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215063 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64519 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150544 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215063 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2285e-08, 215063 } } kg +well_1Control: BHP (at the specified reference elevation): 21462902.30569109 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.94009 +compflowStatistics: Max component CFL number: 81.6575 +Time: 1.11351e+07s, dt:155189s, Cycle: 145 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 9.20e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.58e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 8.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 3.99e-09 ) ; ( R ) = ( 3.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 4.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0540056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670153 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.12903e+07s, dt:159729s, Cycle: 146 +well_1Control: BHP (at the specified reference elevation): 21476024.128197376 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 9.01e-08 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 1.35e-07 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 4.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.35e-04 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 7.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.02e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21489544.244510714 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.055396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065599 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.145e+07s, dt:166717s, Cycle: 147 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.01e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.30e-04 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 6.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0582254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721962 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.16167e+07s, dt:163301s, Cycle: 148 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 9.20e-08 ) ; ( R ) = ( 5.32e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 21503947.369808853 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.45e-04 ) ; ( Rwell ) = ( 9.52e-12 ) ; ( R ) = ( 3.45e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0563341 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649735 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.178e+07s, dt:171512s, Cycle: 149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 9.09e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.33e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 6.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21517907.37388909 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Line search @ 0.500: ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 5.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 6.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 6.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.59e-02 ) ; ( Rwell ) = ( 9.81e-09 ) ; ( R ) = ( 9.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 4.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 6.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 7.91e-09 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.66e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 5.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 5.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 7.25e-09 ) ; ( R ) = ( 9.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 5.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.30e-02 ) ; ( Rwell ) = ( 6.31e-09 ) ; ( R ) = ( 9.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 5.43e-09 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.40e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.96e-02 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 7.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.05e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 4.37e-09 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.59e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 8.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.94e-04 ) ; ( Rwell ) = ( 1.39e-12 ) ; ( R ) = ( 4.94e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0589895 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722787 +coupledFlowAndWells: Time-step required will be decreased based on statwell_1Control: BHP (at the specified reference elevation): 21532365.47480287 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +e change. +Time: 1.19515e+07s, dt:48482.2s, Cycle: 150 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 8.96e-08 ) ; ( R ) = ( 1.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-04 ) ; ( Rwell ) = ( 2.17e-11 ) ; ( R ) = ( 2.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0178335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0197718 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2e+07s, dt:92942.6s, Cycle: 151 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 9.40e-08 ) ; ( R ) = ( 2.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 5.56e-09 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-04 ) ; ( Rwell ) = ( 5.41e-12 ) ; ( R ) = ( 1.26e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0321486 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0391292 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.30517e+07, 1.30911e+07, 1.31313e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 547559, 627156 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.164 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.885365, 728.279 } rm^3 +compflowStatistics, reservoir: Phase mass: { 254.757, 703186 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 46.2754, 211215 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 208.481, 491972 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.03398, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 253.723, 703186 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 254.757, 0 }, { 102.799, 703082 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.29901e+07, 1.30325e+07, 1.30704e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 485930, 566209 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.771 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215079 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64523.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150556 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215079 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22866e-08, 215079 } } kg +compflowStatistics: Max phase CFL number: 1.99848 +compflowStatistics: Max component CFL number: 55.9259 +Time: 1.20929e+07s, dt:131648s, Cycle: 152 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 9.13e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 +well_1Control: BHP (at the specified reference elevation): 21536652.735408276 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +well_1Control: BHP (at the specified reference elevation): 21544640.020316005 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 1.73e-11 ) ; ( R ) = ( 4.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0453009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0572172 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.22246e+07s, dt:149897s, Cycle: 153 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 9.06e-08 ) ; ( R ) = ( 4.91e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 21555876.84023729 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; ( R ) = ( 7.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 4.58e-12 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0513326 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650121 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.23745e+07s, dt:157373s, Cycle: 154 +well_1Control: BHP (at the specified reference elevation): 21568649.05161985 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 9.04e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 4.91e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-04 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 9.11e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.05374 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660115 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25319e+07s, dt:163587s, Cycle: 155 +well_1Control: BHP (at the specified reference elevation): 21581824.963970892 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 8.87e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.05e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; ( R ) = ( 7.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 4.01e-09 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.67e-04 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 2.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0556576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667009 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.26954e+07s, dt:168893s, Cycle: 156 +well_1Control: BHP (at the specified reference elevation): 21595433.09004713 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 8.82e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 6.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; ( R ) = ( 3.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.30e-04 ) ; ( Rwell ) = ( 7.70e-12 ) ; ( R ) = ( 3.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0572304 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0699058 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28643e+07s, dt:135660s, Cycle: 157 +well_1Control: BHP (at the specified reference elevation): 21609570.80054599 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 8.87e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.27e-05 ) ; ( Rwell ) = ( 2.31e-14 ) ; ( R ) = ( 4.27e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.046953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0589079 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.3e+07s, dt:151684s, Cycle: 158 +well_1Control: BHP (at the specified reference elevation): 21621225.291566923 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 9.09e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 7.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 4.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.53e-04 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 3.53e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0511774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600985 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.30979e+07, 1.31373e+07, 1.31773e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 591340, 670756 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.198 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0.954891, 728.243 } rm^3 +compflowStatistics, reservoir: Phase mass: { 276.16, 703179 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 50.7974, 211233 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 225.363, 491946 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.14587, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 275.014, 703179 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 276.16, 0 }, { 112.7, 703064 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.30369e+07, 1.30789e+07, 1.31166e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 530254, 609991 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.782 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215097 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64529.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150568 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215097 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22885e-08, 215097 } } kg +well_1Control: BHP (at the specified reference elevation): 21633957.043770403 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 3.21098 +compflowStatistics: Max component CFL number: 90.8073 +Time: 1.31517e+07s, dt:167477s, Cycle: 159 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 8.88e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 7.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 2.24e-11 ) ; ( R ) = ( 4.68e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0563266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659116 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33192e+07s, dt:174262s, Cycle: 160 +well_1Control: BHP (at the specified reference elevation): 21647746.047438145 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 8.70e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 1.70e-08 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 6.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 1.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.71e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 6.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.41e-02 ) ; ( Rwell ) = ( 8.73e-09 ) ; ( R ) = ( 9.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 5.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.03e-02 ) ; ( Rwell ) = ( 7.56e-09 ) ; ( R ) = ( 9.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 5.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 5.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.44e-02 ) ; ( Rwell ) = ( 6.34e-09 ) ; ( R ) = ( 7.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 5.66e-09 ) ; ( R ) = ( 6.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 5.08e-09 ) ; ( R ) = ( 7.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; ( R ) = ( 7.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 6.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 2.00e-11 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.08e-05 ) ; ( Rwell ) = ( 1.01e-14 ) ; ( R ) = ( 1.08e-05 ) ; + Last LinSolve(iter,res) = ( 8, 1.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0583731 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0710453 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.34934e+07s, dt:172545s, Cycle: 161 +well_1Control: BHP (at the specified reference elevation): 21662159.105521474 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 8.73e-08 ) ; ( R ) = ( 5.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 1.60e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.99e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 6.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 9.14e-09 ) ; ( R ) = ( 9.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 6.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.82e-02 ) ; ( Rwell ) = ( 8.19e-09 ) ; ( R ) = ( 9.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 5.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.64e-02 ) ; ( Rwell ) = ( 6.96e-09 ) ; ( R ) = ( 9.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 5.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 5.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 6.51e-09 ) ; ( R ) = ( 8.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 8.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 5.47e-09 ) ; ( R ) = ( 7.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.52e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; ( R ) = ( 8.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 4.35e-09 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 1.32e-11 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.99e-06 ) ; ( Rwell ) = ( 4.34e-15 ) ; ( R ) = ( 3.99e-06 ) ; + Last LinSolve(iter,res) = ( 8, 9.96e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0582482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728963 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3666e+07s, dt:167913s, Cycle: 162 +well_1Control: BHP (at the specified reference elevation): 21676711.16274751 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 8.90e-08 ) ; ( R ) = ( 5.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 2.99e-07 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.75e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 2.26e-11 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.63e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21690781.249322563 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0561176 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069288 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38339e+07s, dt:166119s, Cycle: 163 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 8.84e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 6.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 4.02e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 7.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0552034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679702 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4e+07s, dt:169394s, Cycle: 164 +well_1Control: BHP (at the specified reference elevation): 21704429.724919103 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 8.67e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 1.70e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.49e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 6.59e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 8.35e-09 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.77e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 6.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.62e-02 ) ; ( Rwell ) = ( 7.91e-09 ) ; ( R ) = ( 9.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.29e-02 ) ; ( Rwell ) = ( 6.68e-09 ) ; ( R ) = ( 9.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.24e-02 ) ; ( Rwell ) = ( 6.02e-09 ) ; ( R ) = ( 7.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.37e-02 ) ; ( Rwell ) = ( 5.44e-09 ) ; ( R ) = ( 7.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 4.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.40e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; ( R ) = ( 8.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.10e-02 ) ; ( Rwell ) = ( 4.44e-09 ) ; ( R ) = ( 7.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; ( R ) = ( 9.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.45e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 7.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.68e-04 ) ; ( Rwell ) = ( 1.58e-11 ) ; ( R ) = ( 6.68e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0561265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658521 +well_1Control: BHP (at the specified reference elevation): 21718484.156288087 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.31416e+07, 1.31809e+07, 1.32208e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 634360, 713613 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.229 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.02022, 728.209 } rm^3 +compflowStatistics, reservoir: Phase mass: { 296.466, 703172 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 55.2178, 211250 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 241.248, 491922 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.42528, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 295.041, 703172 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 296.466, 0 }, { 122.485, 703047 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.30813e+07, 1.31228e+07, 1.31603e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 573921, 653011 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.791 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215114 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64534.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150580 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215114 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22902e-08, 215114 } } kg +compflowStatistics: Max phase CFL number: 3.52651 +compflowStatistics: Max component CFL number: 100.923 +Time: 1.41694e+07s, dt:169394s, Cycle: 165 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 8.74e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 6.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.39e-02 ) ; ( Rwell ) = ( 8.99e-09 ) ; ( R ) = ( 8.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 6.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.42e-02 ) ; ( Rwell ) = ( 8.22e-09 ) ; ( R ) = ( 7.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 5.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.21e-02 ) ; ( Rwell ) = ( 6.62e-09 ) ; ( R ) = ( 9.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 5.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 6.02e-09 ) ; ( R ) = ( 8.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.02e-02 ) ; ( Rwell ) = ( 5.40e-09 ) ; ( R ) = ( 8.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.79e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; ( R ) = ( 7.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.46e-02 ) ; ( Rwell ) = ( 4.24e-09 ) ; ( R ) = ( 7.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 3.70e-09 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 7.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 5.21e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0562844 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715201 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.43388e+07s, dt:166977s, Cycle: 166 +well_1Control: BHP (at the specified reference elevation): 21732601.332384862 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 8.78e-08 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.01e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 9.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-04 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 8.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.80e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21746498.063402154 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0553622 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06906 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45058e+07s, dt:168485s, Cycle: 167 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 8.76e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 4.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.42e-04 ) ; ( Rwell ) = ( 2.49e-11 ) ; ( R ) = ( 5.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0554299 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659427 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.46742e+07s, dt:175257s, Cycle: 168 +well_1Control: BHP (at the specified reference elevation): 21760244.922096662 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 8.58e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 1.60e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.96e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 6.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.48e-02 ) ; ( Rwell ) = ( 9.09e-09 ) ; ( R ) = ( 8.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.53e-02 ) ; ( Rwell ) = ( 8.14e-09 ) ; ( R ) = ( 9.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 5.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.26e-02 ) ; ( Rwell ) = ( 7.50e-09 ) ; ( R ) = ( 8.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.94e-02 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 8.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.75e-02 ) ; ( Rwell ) = ( 5.53e-09 ) ; ( R ) = ( 8.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.58e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; ( R ) = ( 7.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.96e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; ( R ) = ( 7.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.58e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 7.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; ( R ) = ( 5.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.47e-04 ) ; ( Rwell ) = ( 1.37e-11 ) ; ( R ) = ( 2.47e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0574709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683897 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 1.48495e+07s, dt:87628.5s, Cycle: 169 +well_1Control: BHP (at the specified reference elevation): 21774605.191039845 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.61e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.58e-07 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0303879 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0369537 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49371e+07s, dt:62865.3s, Cycle: 170 +well_1Control: BHP (at the specified reference elevation): 21782120.160479534 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 9.01e-08 ) ; ( R ) = ( 1.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.67e-04 ) ; ( Rwell ) = ( 5.43e-12 ) ; ( R ) = ( 4.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0216349 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0263246 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5e+07s, dt:107638s, Cycle: 171 +well_1Control: BHP (at the specified reference elevation): 21787513.086074144 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 9.01e-08 ) ; ( R ) = ( 3.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 6.03e-09 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.53e-06 ) ; ( Rwell ) = ( 2.54e-16 ) ; ( R ) = ( 5.53e-06 ) ; + Last LinSolve(iter,res) = ( 7, 8.45e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0352368 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0433522 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 21796396.159428112 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.31818e+07, 1.32211e+07, 1.32609e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 677195, 756373 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.259 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.08035, 728.178 } rm^3 +compflowStatistics, reservoir: Phase mass: { 315.321, 703166 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 59.2696, 211266 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 256.052, 491900 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.58449, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 313.737, 703166 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 315.321, 0 }, { 131.371, 703032 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.31217e+07, 1.3163e+07, 1.32004e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 617043, 695848 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.8 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.8 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215129 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64538.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150590 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215129 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22918e-08, 215129 } } kg +compflowStatistics: Max phase CFL number: 2.23803 +compflowStatistics: Max component CFL number: 63.848 +Time: 1.51076e+07s, dt:144246s, Cycle: 172 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 8.67e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 4.70e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0471811 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619659 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52519e+07s, dt:156197s, Cycle: 173 +well_1Control: BHP (at the specified reference elevation): 21808188.50152248 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 8.58e-08 ) ; ( R ) = ( 4.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; ( R ) = ( 6.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 4.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-04 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 3.72e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21820813.56385146 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0509583 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675464 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54081e+07s, dt:159935s, Cycle: 174 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 8.48e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.76e-09 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.68e-04 ) ; ( Rwell ) = ( 3.80e-12 ) ; ( R ) = ( 3.68e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 21833848.26980555 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0520077 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619037 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5568e+07s, dt:173297s, Cycle: 175 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 8.54e-08 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 1.58e-08 ) ; ( R ) = ( 1.35e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 6.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 8.33e-09 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; ( R ) = ( 6.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 5.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; ( R ) = ( 6.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; ( R ) = ( 6.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.34e-09 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 8.90e-12 ) ; ( R ) = ( 3.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0561659 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0703072 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.57413e+07s, dt:172792s, Cycle: 176 +well_1Control: BHP (at the specified reference elevation): 21847987.002029315 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 8.54e-08 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.78e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; ( R ) = ( 9.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.14e-02 ) ; ( Rwell ) = ( 3.61e-09 ) ; ( R ) = ( 8.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.27e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; ( R ) = ( 7.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 6.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 6.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.17e-04 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 2.17e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0558549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070608 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.59141e+07s, dt:85895.5s, Cycle: 177 +well_1Control: BHP (at the specified reference elevation): 21862142.911160372 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 8.57e-08 ) ; ( R ) = ( 2.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 9.16e-12 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0290644 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0350557 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6e+07s, dt:128741s, Cycle: 178 +well_1Control: BHP (at the specified reference elevation): 21869394.535877444 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 8.83e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.64e-07 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-03 ) ; ( Rwell ) = ( 8.67e-11 ) ; ( R ) = ( 2.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 1.15e-14 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0415137 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0523843 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.32247e+07, 1.32641e+07, 1.33038e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 719396, 798476 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.29 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.14431, 728.146 } rm^3 +compflowStatistics, reservoir: Phase mass: { 335.554, 703160 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 63.7776, 211282 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 271.776, 491877 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 1.76603, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 333.788, 703160 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 335.554, 0 }, { 141.33, 703016 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.31652e+07, 1.32062e+07, 1.32434e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 659749, 738049 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.81 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.81 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215145 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64543.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150602 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215145 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22935e-08, 215145 } } kg +well_1Control: BHP (at the specified reference elevation): 21879730.973311596 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.63054 +compflowStatistics: Max component CFL number: 76.0088 +Time: 1.61287e+07s, dt:154694s, Cycle: 179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 8.40e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 7.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 2.71e-11 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0497508 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632019 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.62834e+07s, dt:165402s, Cycle: 180 +well_1Control: BHP (at the specified reference elevation): 21892136.765591294 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 8.39e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.29e-09 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 5.07e-11 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0530811 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688976 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.64488e+07s, dt:167157s, Cycle: 181 +well_1Control: BHP (at the specified reference elevation): 21905586.467916988 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 8.50e-08 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 2.61e-11 ) ; ( R ) = ( 6.95e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0536208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06597 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6616e+07s, dt:173829s, Cycle: 182 +well_1Control: BHP (at the specified reference elevation): 21919202.437879674 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 8.51e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 1.51e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 6.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 7.81e-09 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 6.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.08e-02 ) ; ( Rwell ) = ( 6.84e-09 ) ; ( R ) = ( 9.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.47e-02 ) ; ( Rwell ) = ( 6.58e-09 ) ; ( R ) = ( 8.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.49e-02 ) ; ( Rwell ) = ( 5.30e-09 ) ; ( R ) = ( 8.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; ( R ) = ( 9.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.47e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; ( R ) = ( 8.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 8.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.57e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 7.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 7.08e-12 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0554419 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708137 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.67898e+07s, dt:172492s, Cycle: 183 +well_1Control: BHP (at the specified reference elevation): 21933136.480126172 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 8.36e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 1.35e-08 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.76e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 6.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.23e-02 ) ; ( Rwell ) = ( 8.08e-09 ) ; ( R ) = ( 9.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 5.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 5.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 6.44e-09 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 5.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.83e-02 ) ; ( Rwell ) = ( 5.89e-09 ) ; ( R ) = ( 8.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 5.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.01e-02 ) ; ( Rwell ) = ( 5.30e-09 ) ; ( R ) = ( 9.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 4.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; ( R ) = ( 8.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.43e-04 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 6.43e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0548181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660462 +Time: 1.69623e+07s, dt:37684.3s, Cycle: 184 +well_1Control: BHP (at the specified reference elevation): 21946867.483685106 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 8.30e-08 ) ; ( R ) = ( 1.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.26e-03 ) ; ( Rwell ) = ( 7.20e-10 ) ; ( R ) = ( 9.26e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-04 ) ; ( Rwell ) = ( 3.51e-12 ) ; ( R ) = ( 1.05e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0136752 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0155451 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.7e+07s, dt:75368.6s, Cycle: 185 +well_1Control: BHP (at the specified reference elevation): 21950123.134618495 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 9.00e-08 ) ; ( R ) = ( 2.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.50e-04 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 4.50e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0244197 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0312208 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.32641e+07, 1.33035e+07, 1.33431e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 760936, 839949 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.318 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.20277, 728.116 } rm^3 +compflowStatistics, reservoir: Phase mass: { 354.212, 703154 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 68.0245, 211298 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 286.188, 491856 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.03015, 0.0675014 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 352.182, 703154 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 354.212, 0 }, { 150.661, 703001 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.32051e+07, 1.32457e+07, 1.32828e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 701916, 779591 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.819 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.819 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215160 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64548.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150612 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215160 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2295e-08, 215160 } } kg +well_1Control: BHP (at the specified reference elevation): 21956336.92388681 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.52662 +compflowStatistics: Max component CFL number: 44.3074 +Time: 1.70754e+07s, dt:119505s, Cycle: 186 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 8.59e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 6.63e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.55e-03 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 4.96e-10 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.66e-03 ) ; ( Rwell ) = ( 1.40e-10 ) ; ( R ) = ( 7.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.11e-03 ) ; ( Rwell ) = ( 5.79e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.84e-03 ) ; ( Rwell ) = ( 8.65e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.63e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 1.24e-10 ) ; ( R ) = ( 7.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-03 ) ; ( Rwell ) = ( 5.43e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 8.11e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.68e-03 ) ; ( Rwell ) = ( 9.45e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 1.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 1.09e-10 ) ; ( R ) = ( 6.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 5.09e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 7.60e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 8.86e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.66e-03 ) ; ( Rwell ) = ( 9.49e-09 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.25e-03 ) ; ( Rwell ) = ( 9.65e-11 ) ; ( R ) = ( 6.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.84e-05 ) ; ( Rwell ) = ( 1.60e-13 ) ; ( R ) = ( 6.84e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0379172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0506666 +Time: 1.71949e+07s, dt:119505s, Cycle: 187 +well_1Control: BHP (at the specified reference elevation): 21965989.478574276 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 8.41e-08 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 5.13e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 6.45e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.23e-04 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 4.23e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0384609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0481415 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.73144e+07s, dt:150924s, Cycle: 188 +well_1Control: BHP (at the specified reference elevation): 21975720.09563387 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 8.48e-08 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 7.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 8.92e-12 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0477436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624384 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.74653e+07s, dt:162636s, Cycle: 189 +well_1Control: BHP (at the specified reference elevation): 21987692.912736535 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 8.26e-08 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.75e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 6.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.19e-04 ) ; ( Rwell ) = ( 2.68e-11 ) ; ( R ) = ( 3.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0512881 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633665 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.76279e+07s, dt:173603s, Cycle: 190 +well_1Control: BHP (at the specified reference elevation): 22000557.656847686 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 8.23e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 1.37e-08 ) ; ( R ) = ( 1.83e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.12e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 6.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 7.66e-09 ) ; ( R ) = ( 8.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 5.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 7.04e-09 ) ; ( R ) = ( 7.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.55e-02 ) ; ( Rwell ) = ( 5.83e-09 ) ; ( R ) = ( 9.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.26e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.03e-02 ) ; ( Rwell ) = ( 5.21e-09 ) ; ( R ) = ( 9.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.98e-02 ) ; ( Rwell ) = ( 4.50e-09 ) ; ( R ) = ( 8.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.83e-02 ) ; ( Rwell ) = ( 4.14e-09 ) ; ( R ) = ( 7.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; ( R ) = ( 6.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; ( R ) = ( 7.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.36e-04 ) ; ( Rwell ) = ( 2.98e-12 ) ; ( R ) = ( 5.36e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0545478 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665308 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 1.78015e+07s, dt:86801.6s, Cycle: 191 +well_1Control: BHP (at the specified reference elevation): 22014376.49666556 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 8.27e-08 ) ; ( R ) = ( 2.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.87e-04 ) ; ( Rwell ) = ( 4.25e-11 ) ; ( R ) = ( 5.87e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0281097 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0359694 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.78883e+07s, dt:111658s, Cycle: 192 +well_1Control: BHP (at the specified reference elevation): 22021453.582101032 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 3.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.77e-09 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-05 ) ; ( Rwell ) = ( 8.59e-15 ) ; ( R ) = ( 2.96e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0351108 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0444869 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8e+07s, dt:147497s, Cycle: 193 +well_1Control: BHP (at the specified reference elevation): 22030416.23026223 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 8.33e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 9.36e-09 ) ; ( R ) = ( 6.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 5.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0461138 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.060395 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.33082e+07, 1.33475e+07, 1.33871e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 802239, 881168 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.351 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.268, 728.083 } rm^3 +compflowStatistics, reservoir: Phase mass: { 375.207, 703148 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 72.8453, 211315 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 302.362, 491833 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.22147, 0.0674985 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 372.986, 703148 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 375.207, 0 }, { 161.365, 702984 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.32497e+07, 1.329e+07, 1.33269e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 743617, 820894 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.828 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.828 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215177 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64553.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150624 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215177 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22968e-08, 215177 } } kg +well_1Control: BHP (at the specified reference elevation): 22042060.344568208 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.93598 +compflowStatistics: Max component CFL number: 86.2967 +Time: 1.81475e+07s, dt:162348s, Cycle: 194 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 8.19e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 6.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 4.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-04 ) ; ( Rwell ) = ( 3.24e-11 ) ; ( R ) = ( 2.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0505974 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.062058 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.83098e+07s, dt:175632s, Cycle: 195 +well_1Control: BHP (at the specified reference elevation): 22054794.017443173 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 8.14e-08 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 2.79e-08 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 6.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.43e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 8.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.77e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; ( R ) = ( 8.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.06e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; ( R ) = ( 8.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 4.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.04e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; ( R ) = ( 8.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; ( R ) = ( 6.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.66e-04 ) ; ( Rwell ) = ( 1.47e-12 ) ; ( R ) = ( 2.66e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0545588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681145 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 1.84855e+07s, dt:87816s, Cycle: 196 +well_1Control: BHP (at the specified reference elevation): 22068731.939623095 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 8.22e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.13e-04 ) ; ( Rwell ) = ( 1.12e-10 ) ; ( R ) = ( 8.13e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22075902.86728727 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0284189 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0358731 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.85733e+07s, dt:130101s, Cycle: 197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 7.36e-09 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-05 ) ; ( Rwell ) = ( 8.59e-15 ) ; ( R ) = ( 1.23e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0403111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0506997 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.87034e+07s, dt:159401s, Cycle: 198 +well_1Control: BHP (at the specified reference elevation): 22086183.713384815 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 8.19e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 6.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.42e-04 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 6.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0492759 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641228 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.88628e+07s, dt:137206s, Cycle: 199 +well_1Control: BHP (at the specified reference elevation): 22098641.191183988 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 8.09e-08 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 8.09e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.25e-04 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 1.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0424677 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0552076 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9e+07s, dt:159705s, Cycle: 200 +well_1Control: BHP (at the specified reference elevation): 22109489.82717725 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 8.18e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-04 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 3.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0495379 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629252 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.33494e+07, 1.33887e+07, 1.34282e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 842857, 921731 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.38 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.3286, 728.052 } rm^3 +compflowStatistics, reservoir: Phase mass: { 394.887, 703143 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 77.5417, 211331 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 317.346, 491812 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.39328, 0.0674966 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 392.494, 703143 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 394.887, 0 }, { 171.613, 702968 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.32913e+07, 1.33312e+07, 1.3368e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 784782, 861511 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.838 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.838 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215193 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64557.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150635 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215193 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22984e-08, 215193 } } kg +well_1Control: BHP (at the specified reference elevation): 22122152.451601453 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 3.14566 +compflowStatistics: Max component CFL number: 93.0254 +Time: 1.91597e+07s, dt:171243s, Cycle: 201 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 8.20e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 1.28e-08 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 6.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 7.43e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 5.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.88e-02 ) ; ( Rwell ) = ( 6.45e-09 ) ; ( R ) = ( 7.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 5.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 5.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.33e-02 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 7.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; ( R ) = ( 6.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; ( R ) = ( 5.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.50e-09 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 5.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.75e-04 ) ; ( Rwell ) = ( 4.53e-12 ) ; ( R ) = ( 6.75e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0525747 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691208 +Time: 1.93309e+07s, dt:171243s, Cycle: 202 +well_1Control: BHP (at the specified reference elevation): 22135536.391791843 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 8.08e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 1.25e-08 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 7.06e-09 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; ( R ) = ( 4.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 3.39e-09 ) ; ( R ) = ( 4.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; ( R ) = ( 3.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.73e-04 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 2.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.052407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651364 +Time: 1.95022e+07s, dt:171243s, Cycle: 203 +well_1Control: BHP (at the specified reference elevation): 22148830.256506167 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 1.27e-08 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 6.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.06e-02 ) ; ( Rwell ) = ( 6.90e-09 ) ; ( R ) = ( 9.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.96e-02 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 8.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 5.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 5.18e-09 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.20e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; ( R ) = ( 8.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.72e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 7.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 7.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.40e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; ( R ) = ( 7.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; ( R ) = ( 6.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 4.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.052246 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655517 +Time: 1.96734e+07s, dt:171243s, Cycle: 204 +well_1Control: BHP (at the specified reference elevation): 22162238.760706883 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 8.08e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 2.27e-07 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.64e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 7.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 6.92e-09 ) ; ( R ) = ( 1.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 6.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 7.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 6.27e-09 ) ; ( R ) = ( 9.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 6.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.94e-02 ) ; ( Rwell ) = ( 5.24e-09 ) ; ( R ) = ( 9.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.26e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 6.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 6.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.68e-02 ) ; ( Rwell ) = ( 4.68e-09 ) ; ( R ) = ( 9.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 5.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 6.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.16e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; ( R ) = ( 9.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.18e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 5.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.03e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; ( R ) = ( 8.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 4.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.75e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 6.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 6.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; ( R ) = ( 6.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 5.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 1.51e-11 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0525494 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659182 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 1.98447e+07s, dt:85621.5s, Cycle: 205 +well_1Control: BHP (at the specified reference elevation): 22175714.082503714 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 8.12e-08 ) ; ( R ) = ( 2.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.66e-10 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-05 ) ; ( Rwell ) = ( 7.24e-15 ) ; ( R ) = ( 2.00e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.96e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22182677.214731008 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0275073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0332448 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.99303e+07s, dt:69701.6s, Cycle: 206 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 8.39e-08 ) ; ( R ) = ( 1.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 1.91e-12 ) ; ( R ) = ( 4.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0222171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0286592 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2e+07s, dt:114966s, Cycle: 207 +well_1Control: BHP (at the specified reference elevation): 22188326.387963913 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 8.36e-08 ) ; ( R ) = ( 3.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 5.73e-09 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.61e-04 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 7.61e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0349987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0458136 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.33879e+07, 1.34272e+07, 1.34667e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 883295, 962143 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.408 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.38532, 728.023 } rm^3 +compflowStatistics, reservoir: Phase mass: { 413.457, 703138 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 81.9073, 211346 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 331.55, 491792 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.46824, 0.0674954 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 410.989, 703138 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 413.457, 0 }, { 181.288, 702954 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.33301e+07, 1.33698e+07, 1.34066e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 825452, 901951 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.846 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.846 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215207 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64562.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150645 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215207 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22999e-08, 215207 } } kg +well_1Control: BHP (at the specified reference elevation): 22197287.702694003 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.25581 +compflowStatistics: Max component CFL number: 66.6888 +Time: 2.0115e+07s, dt:149374s, Cycle: 208 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 8.03e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 9.02e-09 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.15e-04 ) ; ( Rwell ) = ( 8.77e-12 ) ; ( R ) = ( 6.15e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0453711 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602387 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.02643e+07s, dt:164684s, Cycle: 209 +well_1Control: BHP (at the specified reference elevation): 22208710.185525842 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 7.88e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.06e-02 ) ; ( Rwell ) = ( 1.06e-08 ) ; ( R ) = ( 8.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 7.14e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.049863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652761 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.0429e+07s, dt:172442s, Cycle: 210 +well_1Control: BHP (at the specified reference elevation): 22221409.35020573 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 7.94e-08 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 6.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.92e-02 ) ; ( Rwell ) = ( 6.57e-09 ) ; ( R ) = ( 7.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 5.29e-09 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.46e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; ( R ) = ( 7.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; ( R ) = ( 7.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 6.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; ( R ) = ( 5.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 8.29e-12 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0520463 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659744 +Time: 2.06015e+07s, dt:172442s, Cycle: 211 +well_1Control: BHP (at the specified reference elevation): 22234820.02741456 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 8.00e-08 ) ; ( R ) = ( 4.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 1.41e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 6.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.06e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 9.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.67e-02 ) ; ( Rwell ) = ( 5.93e-09 ) ; ( R ) = ( 8.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 5.34e-09 ) ; ( R ) = ( 7.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 6.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.57e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 7.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.11e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; ( R ) = ( 7.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 6.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; ( R ) = ( 5.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.83e-04 ) ; ( Rwell ) = ( 8.78e-12 ) ; ( R ) = ( 1.83e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0519775 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694666 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 2.07739e+07s, dt:86221.1s, Cycle: 212 +well_1Control: BHP (at the specified reference elevation): 22248198.73764922 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 7.97e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 9.02e-10 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 7.06e-12 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.026979 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0339038 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.08601e+07s, dt:131389s, Cycle: 213 +well_1Control: BHP (at the specified reference elevation): 22255083.059242964 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 8.20e-08 ) ; ( R ) = ( 3.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 6.02e-08 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.72e-04 ) ; ( Rwell ) = ( 7.41e-14 ) ; ( R ) = ( 3.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22265203.034885824 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0394571 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518399 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.09915e+07s, dt:8480.8s, Cycle: 214 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 7.91e-08 ) ; ( R ) = ( 2.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.18e-11 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.68e-06 ) ; ( Rwell ) = ( 1.84e-14 ) ; ( R ) = ( 5.68e-06 ) ; + Last LinSolve(iter,res) = ( 9, 6.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00358476 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00341878 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 2.1e+07s, dt:16961.6s, Cycle: 215 +well_1Control: BHP (at the specified reference elevation): 22265899.389642425 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 8.43e-08 ) ; ( R ) = ( 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 3.62e-11 ) ; ( R ) = ( 8.21e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-03 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 6.73e-11 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.93e-06 ) ; ( Rwell ) = ( 6.53e-13 ) ; ( R ) = ( 6.93e-06 ) ; + Last LinSolve(iter,res) = ( 8, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00560747 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00680868 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +well_1Control: BHP (at the specified reference elevation): 22267277.16998536 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.34238e+07, 1.34631e+07, 1.35026e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 923078, 1.00188e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.435 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.43787, 727.997 } rm^3 +compflowStatistics, reservoir: Phase mass: { 430.799, 703134 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 86.1163, 211361 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 344.682, 491774 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.66463, 0.0674947 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 428.134, 703134 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 430.799, 0 }, { 190.616, 702940 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.33664e+07, 1.34058e+07, 1.34424e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 865757, 941735 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.854 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.854 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215221 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64566.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150655 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215221 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23013e-08, 215221 } } kg +compflowStatistics: Max phase CFL number: 0.328709 +compflowStatistics: Max component CFL number: 9.80115 +Time: 2.1017e+07s, dt:33923.2s, Cycle: 216 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.96e-03 ) ; ( Rwell ) = ( 8.35e-08 ) ; ( R ) = ( 9.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.45e-03 ) ; ( Rwell ) = ( 4.91e-10 ) ; ( R ) = ( 8.45e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 4.27e-13 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0106478 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0140464 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 2.10509e+07s, dt:67846.4s, Cycle: 217 +well_1Control: BHP (at the specified reference elevation): 22269981.00857503 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 8.19e-08 ) ; ( R ) = ( 2.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.95e-04 ) ; ( Rwell ) = ( 7.04e-12 ) ; ( R ) = ( 3.95e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0204846 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0271669 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.11187e+07s, dt:114593s, Cycle: 218 +well_1Control: BHP (at the specified reference elevation): 22275268.577224348 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 8.01e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.16e-09 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-05 ) ; ( Rwell ) = ( 4.31e-14 ) ; ( R ) = ( 1.85e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.46e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0343603 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0462535 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.12333e+07s, dt:148083s, Cycle: 219 +well_1Control: BHP (at the specified reference elevation): 22284096.35860449 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 7.91e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 8.51e-09 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.53e-04 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 4.53e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0443172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0628814 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.13814e+07s, dt:158852s, Cycle: 220 +well_1Control: BHP (at the specified reference elevation): 22295410.42568665 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 7.84e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 9.80e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.33e-04 ) ; ( Rwell ) = ( 2.31e-11 ) ; ( R ) = ( 4.33e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0474172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0634282 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.15403e+07s, dt:169458s, Cycle: 221 +well_1Control: BHP (at the specified reference elevation): 22307646.565880775 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 7.90e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 9.62e-09 ) ; ( R ) = ( 6.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-04 ) ; ( Rwell ) = ( 3.13e-11 ) ; ( R ) = ( 3.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0504246 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671915 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17097e+07s, dt:174116s, Cycle: 222 +well_1Control: BHP (at the specified reference elevation): 22320576.692667603 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 7.82e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.01e-02 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 9.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 5.65e-09 ) ; ( R ) = ( 8.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 7.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; ( R ) = ( 8.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; ( R ) = ( 5.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 6.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.66e-04 ) ; ( Rwell ) = ( 8.49e-12 ) ; ( R ) = ( 2.66e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0516296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069607 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 2.18838e+07s, dt:87057.8s, Cycle: 223 +well_1Control: BHP (at the specified reference elevation): 22333825.28871166 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 7.79e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 7.38e-11 ) ; ( R ) = ( 8.47e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0269064 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0342991 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.19709e+07s, dt:29109.7s, Cycle: 224 +well_1Control: BHP (at the specified reference elevation): 22340675.894302398 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.35e-03 ) ; ( Rwell ) = ( 8.06e-08 ) ; ( R ) = ( 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.19e-03 ) ; ( Rwell ) = ( 3.21e-10 ) ; ( R ) = ( 7.19e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.37e-05 ) ; ( Rwell ) = ( 8.88e-12 ) ; ( R ) = ( 7.37e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00959225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0117991 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 2.2e+07s, dt:58219.5s, Cycle: 225 +well_1Control: BHP (at the specified reference elevation): 22343026.371919706 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 8.26e-08 ) ; ( R ) = ( 1.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 2.66e-10 ) ; ( R ) = ( 7.01e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-04 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 2.45e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0180549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0246883 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.34649e+07, 1.35042e+07, 1.35437e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 962580, 1.04136e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.464 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.49806, 727.966 } rm^3 +compflowStatistics, reservoir: Phase mass: { 450.815, 703130 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 91.0497, 211377 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 359.765, 491753 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 2.86106, 0.0674944 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 447.954, 703129 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 450.815, 0 }, { 201.387, 702924 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.3408e+07, 1.34471e+07, 1.34836e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 905660, 981237 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.863 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.863 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215237 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64571 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150666 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215237 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23029e-08, 215237 } } kg +well_1Control: BHP (at the specified reference elevation): 22347625.102460988 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.11997 +compflowStatistics: Max component CFL number: 33.494 +Time: 2.20582e+07s, dt:102416s, Cycle: 226 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 8.08e-08 ) ; ( R ) = ( 3.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; ( R ) = ( 3.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.03e-06 ) ; ( Rwell ) = ( 8.78e-15 ) ; ( R ) = ( 4.03e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.39e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0303599 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0416972 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.21606e+07s, dt:140210s, Cycle: 227 +well_1Control: BHP (at the specified reference elevation): 22355513.0397721 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 7.88e-08 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 6.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-04 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 1.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0414392 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578936 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.23008e+07s, dt:158483s, Cycle: 228 +well_1Control: BHP (at the specified reference elevation): 22366086.64895799 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 7.71e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 9.32e-09 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; ( R ) = ( 3.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.99e-04 ) ; ( Rwell ) = ( 3.07e-11 ) ; ( R ) = ( 3.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0467203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064218 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.24593e+07s, dt:167718s, Cycle: 229 +well_1Control: BHP (at the specified reference elevation): 22378088.99609838 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 7.74e-08 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 9.66e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.46e-04 ) ; ( Rwell ) = ( 2.57e-11 ) ; ( R ) = ( 7.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0492851 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660624 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.2627e+07s, dt:174253s, Cycle: 230 +well_1Control: BHP (at the specified reference elevation): 22390807.533325963 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.96e-02 ) ; ( Rwell ) = ( 6.57e-09 ) ; ( R ) = ( 7.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.05e-02 ) ; ( Rwell ) = ( 5.35e-09 ) ; ( R ) = ( 8.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; ( R ) = ( 7.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 4.23e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 6.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 4.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.77e-04 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 5.77e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.05103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691996 +Time: 2.28013e+07s, dt:174253s, Cycle: 231 +well_1Control: BHP (at the specified reference elevation): 22403972.483311206 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 7.71e-08 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 1.14e-08 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.42e-02 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 9.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 5.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 5.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.26e-02 ) ; ( Rwell ) = ( 5.29e-09 ) ; ( R ) = ( 9.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.07e-02 ) ; ( Rwell ) = ( 4.66e-09 ) ; ( R ) = ( 9.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.88e-02 ) ; ( Rwell ) = ( 4.29e-09 ) ; ( R ) = ( 7.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.53e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 7.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 2.83e-11 ) ; ( R ) = ( 6.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0508455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677005 +Time: 2.29756e+07s, dt:24447.7s, Cycle: 232 +well_1Control: BHP (at the specified reference elevation): 22417065.349946115 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 7.67e-08 ) ; ( R ) = ( 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.86e-03 ) ; ( Rwell ) = ( 2.06e-10 ) ; ( R ) = ( 5.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-04 ) ; ( Rwell ) = ( 2.83e-12 ) ; ( R ) = ( 1.88e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00842335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00995471 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 2.3e+07s, dt:48895.4s, Cycle: 233 +well_1Control: BHP (at the specified reference elevation): 22419039.8041125 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 8.24e-08 ) ; ( R ) = ( 1.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.90e-03 ) ; ( Rwell ) = ( 1.90e-10 ) ; ( R ) = ( 6.90e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.44e-05 ) ; ( Rwell ) = ( 3.03e-13 ) ; ( R ) = ( 4.44e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0149518 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0194336 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.35035e+07, 1.35428e+07, 1.35822e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.00149e+06, 1.08024e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.492 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.55409, 727.938 } rm^3 +compflowStatistics, reservoir: Phase mass: { 469.605, 703126 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 95.7183, 211392 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 373.886, 491734 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 3.11476, 0.0674944 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 466.49, 703125 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 469.605, 0 }, { 211.888, 702910 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.3447e+07, 1.34858e+07, 1.35221e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 945118, 1.02015e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.872 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.872 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215251 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64575.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150676 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215251 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23045e-08, 215251 } } kg +well_1Control: BHP (at the specified reference elevation): 22422899.886519648 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.926027 +compflowStatistics: Max component CFL number: 28.0146 +Time: 2.30489e+07s, dt:94317.1s, Cycle: 234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 8.05e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 9.24e-10 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-04 ) ; ( Rwell ) = ( 6.03e-12 ) ; ( R ) = ( 2.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0280385 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.038709 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.31432e+07s, dt:134357s, Cycle: 235 +well_1Control: BHP (at the specified reference elevation): 22430190.767914727 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 7.88e-08 ) ; ( R ) = ( 3.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 6.58e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.82e-04 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 2.82e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0391136 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0540157 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.32776e+07s, dt:158483s, Cycle: 236 +well_1Control: BHP (at the specified reference elevation): 22440312.170906715 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 7.67e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 8.36e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 1.87e-11 ) ; ( R ) = ( 6.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0460555 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06088 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.34361e+07s, dt:173557s, Cycle: 237 +well_1Control: BHP (at the specified reference elevation): 22452198.841551416 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 7.64e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.34e-02 ) ; ( Rwell ) = ( 1.42e-07 ) ; ( R ) = ( 9.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; ( R ) = ( 5.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.25e-04 ) ; ( Rwell ) = ( 6.56e-12 ) ; ( R ) = ( 6.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0502861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674284 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.36096e+07s, dt:177915s, Cycle: 238 +well_1Control: BHP (at the specified reference elevation): 22465176.787452072 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 7.61e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 6.09e-09 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; ( R ) = ( 9.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 5.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 4.84e-09 ) ; ( R ) = ( 7.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; ( R ) = ( 7.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 6.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.07e-04 ) ; ( Rwell ) = ( 2.47e-11 ) ; ( R ) = ( 7.07e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0513718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706842 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.37875e+07s, dt:176763s, Cycle: 239 +well_1Control: BHP (at the specified reference elevation): 22478484.73894723 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 7.61e-08 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.10e-02 ) ; ( Rwell ) = ( 6.10e-09 ) ; ( R ) = ( 9.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 5.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; ( R ) = ( 6.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 5.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; ( R ) = ( 6.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.92e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; ( R ) = ( 7.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 7.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.05e-02 ) ; ( Rwell ) = ( 3.21e-09 ) ; ( R ) = ( 7.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.25e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; ( R ) = ( 8.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.71e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; ( R ) = ( 7.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.13e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 7.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.051012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069472 +Time: 2.39643e+07s, dt:35712.6s, Cycle: 240 +well_1Control: BHP (at the specified reference elevation): 22491787.37949268 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 7.65e-08 ) ; ( R ) = ( 1.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.72e-03 ) ; ( Rwell ) = ( 3.96e-10 ) ; ( R ) = ( 8.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-04 ) ; ( Rwell ) = ( 9.84e-12 ) ; ( R ) = ( 1.38e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0115597 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0138653 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 2.4e+07s, dt:71425.2s, Cycle: 241 +well_1Control: BHP (at the specified reference elevation): 22494629.044869307 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 8.09e-08 ) ; ( R ) = ( 2.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.93e-04 ) ; ( Rwell ) = ( 2.56e-12 ) ; ( R ) = ( 3.93e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0210828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0280004 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.3543e+07, 1.35823e+07, 1.36217e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.04016e+06, 1.11888e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.521 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.61145, 727.91 } rm^3 +compflowStatistics, reservoir: Phase mass: { 488.989, 703122 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 100.614, 211408 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 388.375, 491714 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 3.31557, 0.0674948 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 485.673, 703122 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 488.989, 0 }, { 222.737, 702895 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.34869e+07, 1.35254e+07, 1.35616e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 984117, 1.05882e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.881 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.881 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215266 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64579.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150687 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215266 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2306e-08, 215266 } } kg +well_1Control: BHP (at the specified reference elevation): 22500144.571579233 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.34226 +compflowStatistics: Max component CFL number: 40.7516 +Time: 2.40714e+07s, dt:119041s, Cycle: 242 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 7.85e-08 ) ; ( R ) = ( 3.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 4.70e-09 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-04 ) ; ( Rwell ) = ( 7.59e-12 ) ; ( R ) = ( 2.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0345347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0476338 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.41905e+07s, dt:151262s, Cycle: 243 +well_1Control: BHP (at the specified reference elevation): 22509134.257417336 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 7.67e-08 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 7.76e-09 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-03 ) ; ( Rwell ) = ( 8.92e-12 ) ; ( R ) = ( 1.19e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.12e-06 ) ; ( Rwell ) = ( 6.16e-15 ) ; ( R ) = ( 7.12e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0434521 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578324 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.43417e+07s, dt:171088s, Cycle: 244 +well_1Control: BHP (at the specified reference elevation): 22520420.97389336 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 7.57e-08 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.58e-02 ) ; ( Rwell ) = ( 5.50e-09 ) ; ( R ) = ( 9.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.61e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 8.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 4.35e-09 ) ; ( R ) = ( 5.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 6.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.10e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 8.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 6.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; ( R ) = ( 6.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 4.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.18e-04 ) ; ( Rwell ) = ( 1.54e-11 ) ; ( R ) = ( 7.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0490306 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663783 +Time: 2.45128e+07s, dt:171088s, Cycle: 245 +well_1Control: BHP (at the specified reference elevation): 22533108.792810097 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 7.52e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 9.88e-09 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 5.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 5.36e-09 ) ; ( R ) = ( 7.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 4.16e-09 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 4.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.29e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 8.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; ( R ) = ( 7.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; ( R ) = ( 6.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.34e-04 ) ; ( Rwell ) = ( 1.63e-11 ) ; ( R ) = ( 3.34e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0489091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668651 +Time: 2.46839e+07s, dt:171088s, Cycle: 246 +well_1Control: BHP (at the specified reference elevation): 22545882.78299515 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 7.57e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 5.50e-08 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.82e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; ( R ) = ( 7.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 5.66e-08 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.69e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 5.72e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 5.72e-08 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.03e-04 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 5.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0487586 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661938 +Time: 2.4855e+07s, dt:145008s, Cycle: 247 +well_1Control: BHP (at the specified reference elevation): 22558579.460045353 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 7.52e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 6.67e-09 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 3.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.05e-04 ) ; ( Rwell ) = ( 3.26e-11 ) ; ( R ) = ( 4.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0418625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0562926 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.5e+07s, dt:166781s, Cycle: 248 +well_1Control: BHP (at the specified reference elevation): 22569512.319162957 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 7.64e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 9.20e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.59e-04 ) ; ( Rwell ) = ( 2.38e-11 ) ; ( R ) = ( 5.59e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0473416 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064139 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.35847e+07, 1.3624e+07, 1.36634e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.07845e+06, 1.15713e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.552 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.67182, 727.88 } rm^3 +compflowStatistics, reservoir: Phase mass: { 509.561, 703118 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 105.983, 211424 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 403.578, 491694 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 3.67237, 0.0674956 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 505.889, 703118 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 509.561, 0 }, { 234.551, 702879 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.35292e+07, 1.35673e+07, 1.36034e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.02275e+06, 1.09711e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.89 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.89 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215282 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64584.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150698 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215282 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23077e-08, 215282 } } kg +well_1Control: BHP (at the specified reference elevation): 22581834.9341349 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 3.08006 +compflowStatistics: Max component CFL number: 94.7369 +Time: 2.51668e+07s, dt:176641s, Cycle: 249 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 7.48e-08 ) ; ( R ) = ( 4.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.37e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 5.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.18e-02 ) ; ( Rwell ) = ( 5.94e-09 ) ; ( R ) = ( 8.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.72e-02 ) ; ( Rwell ) = ( 5.26e-09 ) ; ( R ) = ( 8.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.34e-02 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 8.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.23e-02 ) ; ( Rwell ) = ( 3.81e-09 ) ; ( R ) = ( 8.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; ( R ) = ( 8.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; ( R ) = ( 5.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.80e-09 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.91e-04 ) ; ( Rwell ) = ( 9.25e-12 ) ; ( R ) = ( 2.91e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0503554 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0680368 +Time: 2.53434e+07s, dt:176641s, Cycle: 250 +well_1Control: BHP (at the specified reference elevation): 22595018.34385643 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 7.55e-08 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 9.83e-09 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 5.72e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.59e-02 ) ; ( Rwell ) = ( 5.92e-09 ) ; ( R ) = ( 9.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 4.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; ( R ) = ( 7.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 4.76e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.30e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 3.69e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 3.55e-09 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 5.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; ( R ) = ( 6.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 6.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 1.45e-11 ) ; ( R ) = ( 6.52e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0499143 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676475 +Time: 2.55201e+07s, dt:176641s, Cycle: 251 +well_1Control: BHP (at the specified reference elevation): 22608052.65651606 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 7.46e-08 ) ; ( R ) = ( 4.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 9.72e-09 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 5.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 5.41e-09 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 5.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.11e-02 ) ; ( Rwell ) = ( 5.21e-09 ) ; ( R ) = ( 7.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 7.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.49e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; ( R ) = ( 9.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 4.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; ( R ) = ( 6.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.44e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; ( R ) = ( 7.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.36e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.27e-04 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 3.27e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0499003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679435 +Time: 2.56967e+07s, dt:176641s, Cycle: 252 +well_1Control: BHP (at the specified reference elevation): 22621133.1983464 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 7.48e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 9.83e-09 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 5.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 5.70e-09 ) ; ( R ) = ( 7.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 5.19e-09 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 4.53e-09 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.98e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; ( R ) = ( 7.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.46e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 7.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; ( R ) = ( 7.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.33e-04 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.33e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0496868 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670406 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 2.58733e+07s, dt:88320.5s, Cycle: 253 +well_1Control: BHP (at the specified reference elevation): 22634220.76759223 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 7.48e-08 ) ; ( R ) = ( 2.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 2.03e-15 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0260823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0342038 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.59617e+07s, dt:38334.7s, Cycle: 254 +well_1Control: BHP (at the specified reference elevation): 22640963.329953924 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 7.70e-08 ) ; ( R ) = ( 1.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 4.28e-10 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-03 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 1.64e-10 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.80e-06 ) ; ( Rwell ) = ( 2.53e-12 ) ; ( R ) = ( 8.80e-06 ) ; + Last LinSolve(iter,res) = ( 8, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0117546 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0149981 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 2.6e+07s, dt:76669.4s, Cycle: 255 +well_1Control: BHP (at the specified reference elevation): 22643951.42184993 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 7.86e-08 ) ; ( R ) = ( 2.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.71e-04 ) ; ( Rwell ) = ( 4.09e-13 ) ; ( R ) = ( 9.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0222609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0300331 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.36195e+07, 1.36587e+07, 1.36981e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.11646e+06, 1.19514e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.577 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.72203, 727.855 } rm^3 +compflowStatistics, reservoir: Phase mass: { 526.798, 703114 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 110.46, 211438 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 416.338, 491677 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 3.94686, 0.0674966 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 522.851, 703114 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 526.798, 0 }, { 244.217, 702866 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.35639e+07, 1.3602e+07, 1.36381e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.06098e+06, 1.13512e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.898 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.898 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215296 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64588.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150707 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215296 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2309e-08, 215296 } } kg +well_1Control: BHP (at the specified reference elevation): 22649801.73344691 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.42374 +compflowStatistics: Max component CFL number: 43.3913 +Time: 2.60767e+07s, dt:123788s, Cycle: 256 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 7.70e-08 ) ; ( R ) = ( 3.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 9.98e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.66e-04 ) ; ( Rwell ) = ( 4.07e-12 ) ; ( R ) = ( 7.66e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0349149 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0485119 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.62005e+07s, dt:155639s, Cycle: 257 +well_1Control: BHP (at the specified reference elevation): 22658924.553014167 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 7.43e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 7.37e-09 ) ; ( R ) = ( 6.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.57e-04 ) ; ( Rwell ) = ( 1.35e-11 ) ; ( R ) = ( 5.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0437407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061005 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.63561e+07s, dt:170221s, Cycle: 258 +well_1Control: BHP (at the specified reference elevation): 22670295.073626086 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 7.37e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 9.03e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 5.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 7.39e-12 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0477007 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660568 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.65263e+07s, dt:176863s, Cycle: 259 +well_1Control: BHP (at the specified reference elevation): 22682686.00120446 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 7.34e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 9.96e-09 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 5.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 5.70e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 5.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 6.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 9.88e-12 ) ; ( R ) = ( 2.83e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0494144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663282 +Time: 2.67032e+07s, dt:176863s, Cycle: 260 +well_1Control: BHP (at the specified reference elevation): 22695724.716886543 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 7.42e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 9.96e-09 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 5.55e-09 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 5.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.12e-04 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 3.12e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0492766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658701 +Time: 2.688e+07s, dt:119957s, Cycle: 261 +well_1Control: BHP (at the specified reference elevation): 22708679.054710925 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 7.37e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.75e-09 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.54e-04 ) ; ( Rwell ) = ( 1.05e-11 ) ; ( R ) = ( 3.54e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.034028 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0464051 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.7e+07s, dt:154726s, Cycle: 262 +well_1Control: BHP (at the specified reference elevation): 22717602.045394383 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 7.48e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 6.99e-09 ) ; ( R ) = ( 7.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.50e-04 ) ; ( Rwell ) = ( 1.95e-11 ) ; ( R ) = ( 2.50e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0433283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.060012 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.36599e+07, 1.36992e+07, 1.37385e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.15407e+06, 1.23271e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.606 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.78021, 727.826 } rm^3 +compflowStatistics, reservoir: Phase mass: { 546.928, 703111 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 115.782, 211454 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 431.145, 491657 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 4.25716, 0.0674979 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 542.671, 703111 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 546.928, 0 }, { 255.962, 702850 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.36048e+07, 1.36426e+07, 1.36786e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.09898e+06, 1.17273e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.907 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.907 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215311 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64593.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150718 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215311 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23106e-08, 215311 } } kg +well_1Control: BHP (at the specified reference elevation): 22728996.667389818 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.82136 +compflowStatistics: Max component CFL number: 87.1959 +Time: 2.71547e+07s, dt:170991s, Cycle: 263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 7.40e-08 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 9.21e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 5.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; ( R ) = ( 6.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 4.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; ( R ) = ( 4.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; ( R ) = ( 3.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; ( R ) = ( 4.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 9.69e-12 ) ; ( R ) = ( 3.71e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0474214 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064139 +Time: 2.73257e+07s, dt:170991s, Cycle: 264 +well_1Control: BHP (at the specified reference elevation): 22741459.088661022 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 7.32e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 3.84e-08 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 7.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0472883 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648989 +Time: 2.74967e+07s, dt:170991s, Cycle: 265 +well_1Control: BHP (at the specified reference elevation): 22753812.732446425 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 7.25e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.76e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 5.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 7.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.10e-02 ) ; ( Rwell ) = ( 4.19e-09 ) ; ( R ) = ( 7.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.22e-04 ) ; ( Rwell ) = ( 1.84e-11 ) ; ( R ) = ( 8.22e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.047142 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656526 +Time: 2.76677e+07s, dt:170991s, Cycle: 266 +well_1Control: BHP (at the specified reference elevation): 22766216.036567733 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 7.28e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.89e-02 ) ; ( Rwell ) = ( 8.63e-09 ) ; ( R ) = ( 9.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 5.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 4.73e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 4.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 9.27e-12 ) ; ( R ) = ( 6.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0469937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650745 +Time: 2.78387e+07s, dt:161309s, Cycle: 267 +well_1Control: BHP (at the specified reference elevation): 22778572.3964888 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 7.25e-08 ) ; ( R ) = ( 4.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 7.97e-09 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.37e-04 ) ; ( Rwell ) = ( 5.79e-12 ) ; ( R ) = ( 3.37e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0453617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0610145 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.8e+07s, dt:176405s, Cycle: 268 +well_1Control: BHP (at the specified reference elevation): 22790506.9240807 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 7.42e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 9.87e-09 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 5.16e-09 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 4.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; ( R ) = ( 8.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 4.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.92e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; ( R ) = ( 7.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.44e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 8.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 6.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; ( R ) = ( 7.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 6.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; ( R ) = ( 5.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.55e-04 ) ; ( Rwell ) = ( 9.77e-12 ) ; ( R ) = ( 3.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0483258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0647574 +compflowStatistics, reservoir: Pressure (min, average, max): 1.36978e+07, 1.37371e+07, 1.37764e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.19127e+06, 1.26989e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.634 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.83452, 727.799 } rm^3 +compflowStatistics, reservoir: Phase mass: { 565.866, 703108 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 120.811, 211469 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 445.055, 491639 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 4.62925, 0.0674994 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 561.237, 703108 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 565.866, 0 }, { 267.232, 702836 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.36432e+07, 1.36807e+07, 1.37165e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.13657e+06, 1.20993e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.915 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.915 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215325 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64597.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150728 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215325 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23121e-08, 215325 } } kg +well_1Control: BHP (at the specified reference elevation): 22803296.011215735 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 3.1778 +compflowStatistics: Max component CFL number: 99.0188 +Time: 2.81764e+07s, dt:176405s, Cycle: 269 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 7.26e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-01 ) ; ( Rwell ) = ( 8.51e-09 ) ; ( R ) = ( 1.84e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 5.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 5.22e-09 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.25e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.32e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; ( R ) = ( 9.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.18e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 4.08e-09 ) ; ( R ) = ( 8.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; ( R ) = ( 8.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 7.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 7.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 7.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 6.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 4.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.88e-04 ) ; ( Rwell ) = ( 6.91e-12 ) ; ( R ) = ( 7.88e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0481949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067345 +Time: 2.83528e+07s, dt:176405s, Cycle: 270 +well_1Control: BHP (at the specified reference elevation): 22815893.809871785 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 7.15e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 9.18e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 4.41e-09 ) ; ( R ) = ( 7.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 3.61e-09 ) ; ( R ) = ( 6.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 5.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 2.83e-09 ) ; ( R ) = ( 6.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.35e-04 ) ; ( Rwell ) = ( 5.06e-12 ) ; ( R ) = ( 4.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0480376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064866 +Time: 2.85292e+07s, dt:176405s, Cycle: 271 +well_1Control: BHP (at the specified reference elevation): 22828537.38518838 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 7.17e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 8.80e-09 ) ; ( R ) = ( 1.38e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.95e-02 ) ; ( Rwell ) = ( 4.74e-09 ) ; ( R ) = ( 8.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.51e-04 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 7.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0483779 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652704 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.87056e+07s, dt:184726s, Cycle: 272 +well_1Control: BHP (at the specified reference elevation): 22841350.657781385 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 7.26e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 8.85e-08 ) ; ( R ) = ( 1.65e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.26e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 8.86e-08 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 8.92e-08 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.33e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 4.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.18e-02 ) ; ( Rwell ) = ( 8.93e-08 ) ; ( R ) = ( 9.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.05e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.10e-02 ) ; ( Rwell ) = ( 8.92e-08 ) ; ( R ) = ( 7.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 8.95e-08 ) ; ( R ) = ( 8.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.10e-02 ) ; ( Rwell ) = ( 8.97e-08 ) ; ( R ) = ( 8.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 8.95e-08 ) ; ( R ) = ( 7.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 8.98e-08 ) ; ( R ) = ( 7.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 4.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 8.98e-08 ) ; ( R ) = ( 6.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 8.98e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.67e-04 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0502346 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642523 +Time: 2.88903e+07s, dt:109653s, Cycle: 273 +well_1Control: BHP (at the specified reference elevation): 22854696.410926756 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 7.22e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.64e-04 ) ; ( Rwell ) = ( 4.11e-12 ) ; ( R ) = ( 2.64e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0308343 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0405136 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.9e+07s, dt:152470s, Cycle: 274 +well_1Control: BHP (at the specified reference elevation): 22862799.749918297 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 7.39e-08 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 6.64e-09 ) ; ( R ) = ( 6.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.63e-04 ) ; ( Rwell ) = ( 4.72e-12 ) ; ( R ) = ( 3.63e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.30e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22873794.743135966 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0412896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575702 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.37337e+07, 1.3773e+07, 1.38123e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.22814e+06, 1.30674e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.66 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.88589, 727.774 } rm^3 +compflowStatistics, reservoir: Phase mass: { 583.912, 703105 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 125.7, 211483 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 458.212, 491622 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.075, 0.0675009 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 578.837, 703105 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 583.912, 0 }, { 278.045, 702822 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.36794e+07, 1.37167e+07, 1.37524e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.17374e+06, 1.2468e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.923 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.923 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215339 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64601.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150737 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215339 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23136e-08, 215339 } } kg +compflowStatistics: Max phase CFL number: 2.72905 +compflowStatistics: Max component CFL number: 85.2623 +Time: 2.91525e+07s, dt:172943s, Cycle: 275 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 7.20e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 8.36e-09 ) ; ( R ) = ( 1.38e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 5.45e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.67e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 5.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 3.35e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.71e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; ( R ) = ( 8.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.02e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 8.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 7.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 6.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 5.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.86e-04 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 1.86e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0467403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598917 +Time: 2.93254e+07s, dt:172943s, Cycle: 276 +well_1Control: BHP (at the specified reference elevation): 22886065.36545644 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 7.08e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 8.04e-09 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 5.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 4.93e-09 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; ( R ) = ( 8.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.33e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 7.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; ( R ) = ( 7.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 6.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 9.68e-10 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 8.78e-10 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 3.00e-04 ) ; ( Rwell ) = ( 9.07e-12 ) ; ( R ) = ( 3.00e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0466205 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613647 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 2.94984e+07s, dt:86471.3s, Cycle: 277 +well_1Control: BHP (at the specified reference elevation): 22898441.22751502 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 7.14e-08 ) ; ( R ) = ( 2.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.50e-03 ) ; ( Rwell ) = ( 5.84e-10 ) ; ( R ) = ( 9.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-04 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 2.00e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0246042 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0310066 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.95848e+07s, dt:137554s, Cycle: 278 +well_1Control: BHP (at the specified reference elevation): 22904874.95674847 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 7.42e-08 ) ; ( R ) = ( 3.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 5.06e-09 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.56e-04 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 2.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0375231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0514832 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.97224e+07s, dt:167006s, Cycle: 279 +well_1Control: BHP (at the specified reference elevation): 22914907.059179887 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 7.27e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 7.80e-09 ) ; ( R ) = ( 7.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.32e-04 ) ; ( Rwell ) = ( 2.46e-11 ) ; ( R ) = ( 5.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0451158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.062981 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.98894e+07s, dt:110614s, Cycle: 280 +well_1Control: BHP (at the specified reference elevation): 22926943.683828834 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 7.18e-08 ) ; ( R ) = ( 3.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 3.67e-12 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.34e-06 ) ; ( Rwell ) = ( 3.47e-15 ) ; ( R ) = ( 4.34e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.25e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0300182 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0393768 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3e+07s, dt:156156s, Cycle: 281 +well_1Control: BHP (at the specified reference elevation): 22934912.087828707 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 7.17e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 6.25e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-04 ) ; ( Rwell ) = ( 2.29e-11 ) ; ( R ) = ( 5.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.041943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0577947 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.37705e+07, 1.38097e+07, 1.3849e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.26489e+06, 1.34347e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.686 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.93833, 727.748 } rm^3 +compflowStatistics, reservoir: Phase mass: { 602.461, 703103 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 130.712, 211498 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 471.749, 491605 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.46895, 0.0675026 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 596.992, 703103 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 602.461, 0 }, { 289.172, 702808 } } kg +well_1Control: BHP (at the specified reference elevation): 22945859.109398507 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.37164e+07, 1.37535e+07, 1.37891e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.21066e+06, 1.28355e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.931 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.931 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215353 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64605.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150747 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215353 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2315e-08, 215353 } } kg +compflowStatistics: Max phase CFL number: 2.76219 +compflowStatistics: Max component CFL number: 86.9901 +Time: 3.01562e+07s, dt:176696s, Cycle: 282 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 6.98e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 1.73e-07 ) ; ( R ) = ( 1.63e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 7.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 4.72e-09 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 6.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 6.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 6.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.57e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 7.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 5.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 5.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 5.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.79e-04 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 6.79e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0472998 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06163 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.03329e+07s, dt:192001s, Cycle: 283 +well_1Control: BHP (at the specified reference elevation): 22958363.27159757 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 7.04e-08 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 9.12e-09 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 5.59e-09 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 4.05e-09 ) ; ( R ) = ( 7.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.44e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 9.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 8.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 2.52e-09 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 2.67e-11 ) ; ( R ) = ( 5.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0512377 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683522 +Time: 3.05249e+07s, dt:192001s, Cycle: 284 +well_1Control: BHP (at the specified reference elevation): 22972070.32239416 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 7.10e-08 ) ; ( R ) = ( 4.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 1.95e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.76e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 5.20e-09 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.59e-02 ) ; ( Rwell ) = ( 4.95e-09 ) ; ( R ) = ( 9.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.46e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.63e-02 ) ; ( Rwell ) = ( 4.08e-09 ) ; ( R ) = ( 9.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.86e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.86e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.46e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; ( R ) = ( 9.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.02e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.88e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.22e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; ( R ) = ( 8.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 7.20e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 9.52e-06 ) ; ( Rwell ) = ( 1.46e-15 ) ; ( R ) = ( 9.52e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0517116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659135 +Time: 3.07169e+07s, dt:192001s, Cycle: 285 +well_1Control: BHP (at the specified reference elevation): 22985873.01866866 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 7.14e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 1.11e-08 ) ; ( R ) = ( 1.35e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 5.01e-09 ) ; ( R ) = ( 1.28e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.10e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 4.68e-09 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.47e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 4.46e-09 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.64e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 7.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 5.56e-12 ) ; ( R ) = ( 7.93e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 22999343.41344012 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0510039 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641068 +Time: 3.09089e+07s, dt:91145.4s, Cycle: 286 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 6.97e-08 ) ; ( R ) = ( 2.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 7.39e-10 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-04 ) ; ( Rwell ) = ( 5.35e-12 ) ; ( R ) = ( 1.94e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0253836 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0322268 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.1e+07s, dt:142358s, Cycle: 287 +well_1Control: BHP (at the specified reference elevation): 23006021.08287763 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 7.27e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 5.52e-09 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 7.79e-12 ) ; ( R ) = ( 4.16e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.03775 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0529143 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.38063e+07, 1.38455e+07, 1.38848e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.30111e+06, 1.37967e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.713 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 1.98928, 727.723 } rm^3 +compflowStatistics, reservoir: Phase mass: { 620.615, 703100 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 135.786, 211512 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 484.829, 491588 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 5.85245, 0.0675045 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 614.762, 703100 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 620.615, 0 }, { 300.177, 702794 } } kg +well_1Control: BHP (at the specified reference elevation): 23016166.67371262 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.37525e+07, 1.37894e+07, 1.38249e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.24728e+06, 1.31977e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.939 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.939 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215367 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64610 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150757 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215367 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23164e-08, 215367 } } kg +compflowStatistics: Max phase CFL number: 2.50822 +compflowStatistics: Max component CFL number: 79.0086 +Time: 3.11424e+07s, dt:170025s, Cycle: 288 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 7.07e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 7.70e-09 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.46e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 5.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 7.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 5.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.17e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; ( R ) = ( 9.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.96e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 8.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.79e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 7.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 8.83e-12 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0450056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588935 +Time: 3.13124e+07s, dt:170025s, Cycle: 289 +well_1Control: BHP (at the specified reference elevation): 23028085.122051865 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 6.95e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 7.61e-09 ) ; ( R ) = ( 1.38e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 5.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 4.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 6.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 6.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 7.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 5.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.48e-04 ) ; ( Rwell ) = ( 7.86e-12 ) ; ( R ) = ( 2.48e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0455414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588785 +Time: 3.14824e+07s, dt:170025s, Cycle: 290 +well_1Control: BHP (at the specified reference elevation): 23040207.888218913 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 7.06e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.97e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 9.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 5.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 5.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 6.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 6.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 6.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 5.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 9.65e-10 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.00e-04 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 2.00e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0450329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0577882 +Time: 3.16524e+07s, dt:170025s, Cycle: 291 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 7.02e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 7.61e-09 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; ( R ) = ( 6.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; ( R ) = ( 5.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 4.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. +well_1Control: BHP (at the specified reference elevation): 23052266.458899282 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.60e-04 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 5.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0447796 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0582763 +Time: 3.18225e+07s, dt:170025s, Cycle: 292 +well_1Control: BHP (at the specified reference elevation): 23064259.65445183 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 6.98e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 7.65e-09 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 4.29e-09 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 1.42e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.25e-09 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 9.33e-10 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 8.35e-10 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 1.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 6.77e-10 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 1.51e-04 ) ; ( Rwell ) = ( 1.50e-11 ) ; ( R ) = ( 1.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0446905 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0592323 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 3.19925e+07s, dt:7519.19s, Cycle: 293 +well_1Control: BHP (at the specified reference elevation): 23076233.754602153 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.97e-08 ) ; ( R ) = ( 1.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 4.34e-12 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.10e-06 ) ; ( Rwell ) = ( 1.17e-14 ) ; ( R ) = ( 4.10e-06 ) ; + Last LinSolve(iter,res) = ( 8, 7.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00284597 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00263638 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.2e+07s, dt:15038.4s, Cycle: 294 +well_1Control: BHP (at the specified reference elevation): 23076794.879335884 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.76e-03 ) ; ( Rwell ) = ( 7.38e-08 ) ; ( R ) = ( 3.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 2, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 5.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.59e-11 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-03 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 1.42e-11 ) ; ( R ) = ( 9.54e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-03 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-03 ) ; ( Rwell ) = ( 4.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.17e-03 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 9.17e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-03 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.22e-03 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.76e-03 ) ; ( Rwell ) = ( 9.68e-12 ) ; ( R ) = ( 8.76e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.49e-03 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-03 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.32e-03 ) ; ( Rwell ) = ( 9.74e-12 ) ; ( R ) = ( 8.32e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.94e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 7.94e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.34e-03 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-03 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-03 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 7.58e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.60e-03 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-03 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.24e-03 ) ; ( Rwell ) = ( 9.22e-12 ) ; ( R ) = ( 7.24e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.64e-03 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.91e-03 ) ; ( Rwell ) = ( 8.23e-12 ) ; ( R ) = ( 6.91e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.45e-03 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.10e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 2.10e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.48e-05 ) ; ( Rwell ) = ( 4.50e-13 ) ; ( R ) = ( 1.48e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00523411 +compflowStatistics, reservoir: Pressure (min, average, max): 1.38377e+07, 1.3877e+07, 1.39163e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.33714e+06, 1.41568e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.735 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.03392, 727.701 } rm^3 +compflowStatistics, reservoir: Phase mass: { 636.625, 703098 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 140.232, 211524 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 496.394, 491574 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 6.27641, 0.0675062 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 630.349, 703098 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 636.625, 0 }, { 309.97, 702782 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.37842e+07, 1.38209e+07, 1.38564e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.28361e+06, 1.3558e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.946 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.946 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215379 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64613.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150765 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215379 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23177e-08, 215379 } } kg +well_1Control: BHP (at the specified reference elevation): 23077918.6223597 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.263084 +compflowStatistics: Max component CFL number: 8.31912 +Time: 3.2015e+07s, dt:15038.4s, Cycle: 295 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-03 ) ; ( Rwell ) = ( 7.39e-08 ) ; ( R ) = ( 3.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.25e-11 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.91e-11 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-03 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 4.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 9.52e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 4.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.06e-03 ) ; ( Rwell ) = ( 2.07e-11 ) ; ( R ) = ( 9.06e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.49e-03 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-03 ) ; ( Rwell ) = ( 4.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.62e-03 ) ; ( Rwell ) = ( 1.99e-11 ) ; ( R ) = ( 8.62e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.21e-03 ) ; ( Rwell ) = ( 2.02e-11 ) ; ( R ) = ( 8.21e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.36e-03 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-03 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 7.81e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.27e-03 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.93e-03 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.39e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 7.39e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.16e-03 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-03 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.12e-03 ) ; ( Rwell ) = ( 1.72e-11 ) ; ( R ) = ( 7.12e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-03 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.21e-03 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.89e-03 ) ; ( Rwell ) = ( 1.69e-11 ) ; ( R ) = ( 6.89e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.05e-03 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-03 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-03 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.56e-03 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 6.56e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-03 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-03 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.53e-11 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.05e-06 ) ; ( Rwell ) = ( 2.31e-13 ) ; ( R ) = ( 3.05e-06 ) ; + Last LinSolve(iter,res) = ( 9, 5.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00435291 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00517586 +Time: 3.20301e+07s, dt:15038.4s, Cycle: 296 +well_1Control: BHP (at the specified reference elevation): 23079032.882185243 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 7.33e-08 ) ; ( R ) = ( 3.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 5.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 2.60e-11 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-03 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 2.56e-11 ) ; ( R ) = ( 9.61e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-03 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-03 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.38e-03 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.00e-03 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.20e-03 ) ; ( Rwell ) = ( 2.62e-11 ) ; ( R ) = ( 9.20e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.60e-03 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-03 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.25e-03 ) ; ( Rwell ) = ( 3.90e-11 ) ; ( R ) = ( 8.25e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-03 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-03 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.84e-03 ) ; ( Rwell ) = ( 3.53e-11 ) ; ( R ) = ( 7.84e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-03 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.12e-03 ) ; ( Rwell ) = ( 2.48e-11 ) ; ( R ) = ( 8.12e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.61e-03 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-03 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.80e-03 ) ; ( Rwell ) = ( 2.19e-11 ) ; ( R ) = ( 2.80e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.35e-05 ) ; ( Rwell ) = ( 1.31e-12 ) ; ( R ) = ( 3.35e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00435653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00517472 +Time: 3.20451e+07s, dt:15038.4s, Cycle: 297 +well_1Control: BHP (at the specified reference elevation): 23080141.35512215 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 7.29e-08 ) ; ( R ) = ( 3.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 3.42e-11 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 2, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 5.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 4.10e-11 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 4.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-03 ) ; ( Rwell ) = ( 5.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 4.39e-11 ) ; ( R ) = ( 9.63e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-03 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-03 ) ; ( Rwell ) = ( 4.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-03 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 4.98e-11 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-03 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.24e-03 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 4.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.47e-03 ) ; ( Rwell ) = ( 4.93e-11 ) ; ( R ) = ( 8.47e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.40e-03 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-03 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.34e-03 ) ; ( Rwell ) = ( 3.97e-11 ) ; ( R ) = ( 8.34e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-03 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.59e-03 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 2.59e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.65e-06 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 2.65e-06 ) ; + Last LinSolve(iter,res) = ( 9, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00443726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00521935 +Time: 3.20602e+07s, dt:15038.4s, Cycle: 298 +well_1Control: BHP (at the specified reference elevation): 23081247.625368 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-03 ) ; ( Rwell ) = ( 7.28e-08 ) ; ( R ) = ( 3.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 5.01e-11 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 2, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 5.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.96e-03 ) ; ( Rwell ) = ( 6.74e-11 ) ; ( R ) = ( 9.96e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-03 ) ; ( Rwell ) = ( 5.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 6.00e-11 ) ; ( R ) = ( 9.52e-03 ) ; + Last LinSolve(iter,res) = ( 2, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-03 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 4.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.89e-03 ) ; ( Rwell ) = ( 4.66e-11 ) ; ( R ) = ( 2.89e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.41e-05 ) ; ( Rwell ) = ( 5.83e-13 ) ; ( R ) = ( 1.41e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00448002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00528297 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.20752e+07s, dt:30076.8s, Cycle: 299 +well_1Control: BHP (at the specified reference elevation): 23082356.03301219 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.48e-03 ) ; ( Rwell ) = ( 7.29e-08 ) ; ( R ) = ( 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 2.09e-10 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-04 ) ; ( Rwell ) = ( 1.60e-12 ) ; ( R ) = ( 1.31e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00839042 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0105271 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.21053e+07s, dt:60153.6s, Cycle: 300 +well_1Control: BHP (at the specified reference elevation): 23084553.747514725 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 7.23e-08 ) ; ( R ) = ( 1.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.68e-03 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 1.23e-10 ) ; ( R ) = ( 6.85e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-04 ) ; ( Rwell ) = ( 1.57e-11 ) ; ( R ) = ( 2.99e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0160534 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0207241 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.21654e+07s, dt:113346s, Cycle: 301 +well_1Control: BHP (at the specified reference elevation): 23088859.062852554 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 7.08e-08 ) ; ( R ) = ( 2.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 3.31e-09 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 8.48e-10 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 8.72e-12 ) ; ( R ) = ( 4.20e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0299573 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.040367 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.22788e+07s, dt:157912s, Cycle: 302 +well_1Control: BHP (at the specified reference elevation): 23096870.449033618 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 6.99e-08 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 5.99e-09 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.82e-04 ) ; ( Rwell ) = ( 2.74e-11 ) ; ( R ) = ( 1.82e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0414699 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0547884 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.24367e+07s, dt:184665s, Cycle: 303 +well_1Control: BHP (at the specified reference elevation): 23107891.620488368 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 6.90e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 8.75e-09 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 4.60e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.92e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; ( R ) = ( 9.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.91e-02 ) ; ( Rwell ) = ( 3.65e-09 ) ; ( R ) = ( 8.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.93e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 8.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.33e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 8.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.82e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; ( R ) = ( 7.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 7.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; ( R ) = ( 6.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.00e-04 ) ; ( Rwell ) = ( 1.48e-11 ) ; ( R ) = ( 6.00e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0483344 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644616 +Time: 3.26213e+07s, dt:184665s, Cycle: 304 +well_1Control: BHP (at the specified reference elevation): 23120630.102107927 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 8.41e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 3.86e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; ( R ) = ( 5.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; ( R ) = ( 8.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 6.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 9.83e-10 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 8.75e-10 ) ; ( R ) = ( 5.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 7.80e-10 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 18 + ( Rflow ) = ( 2.89e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.048158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643991 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 3.2806e+07s, dt:92332.4s, Cycle: 305 +well_1Control: BHP (at the specified reference elevation): 23133520.767093927 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 6.89e-08 ) ; ( R ) = ( 2.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 1.85e-10 ) ; ( R ) = ( 5.29e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0252114 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0318907 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.28983e+07s, dt:101657s, Cycle: 306 +well_1Control: BHP (at the specified reference elevation): 23140198.50959666 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 7.15e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.67e-04 ) ; ( Rwell ) = ( 3.06e-11 ) ; ( R ) = ( 8.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0267069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0354101 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.3e+07s, dt:151598s, Cycle: 307 +well_1Control: BHP (at the specified reference elevation): 23147414.271047704 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 7.00e-08 ) ; ( R ) = ( 3.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 5.61e-09 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.64e-04 ) ; ( Rwell ) = ( 1.06e-11 ) ; ( R ) = ( 4.64e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.039412 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0519826 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.38784e+07, 1.39177e+07, 1.39569e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.37308e+06, 1.4516e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.765 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.09164, 727.673 } rm^3 +compflowStatistics, reservoir: Phase mass: { 657.467, 703096 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 146.037, 211540 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 511.43, 491555 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 6.8204, 0.0675086 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 650.646, 703096 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 657.467, 0 }, { 322.733, 702767 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.38252e+07, 1.38617e+07, 1.38971e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.31973e+06, 1.39174e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.955 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.955 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215394 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64618.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150776 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215394 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23193e-08, 215394 } } kg +compflowStatistics: Max phase CFL number: 2.62287 +compflowStatistics: Max component CFL number: 83.5108 +Time: 3.31516e+07s, dt:183000s, Cycle: 308 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 4.47e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 23157894.52446457 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 7.98e-09 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; ( R ) = ( 6.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.35e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; ( R ) = ( 8.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 7.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.33e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 8.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 4.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.85e-04 ) ; ( Rwell ) = ( 2.30e-11 ) ; ( R ) = ( 5.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0474553 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618586 +Time: 3.33346e+07s, dt:183000s, Cycle: 309 +well_1Control: BHP (at the specified reference elevation): 23170599.06925504 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 6.84e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 8.44e-09 ) ; ( R ) = ( 6.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 7.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; ( R ) = ( 6.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.65e-04 ) ; ( Rwell ) = ( 8.46e-12 ) ; ( R ) = ( 4.65e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.047322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0620987 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.35176e+07s, dt:197891s, Cycle: 310 +well_1Control: BHP (at the specified reference elevation): 23183314.68891016 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 6.84e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 9.23e-09 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.76e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; ( R ) = ( 8.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 4.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 4.50e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.43e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; ( R ) = ( 9.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.17e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; ( R ) = ( 9.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.12e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 9.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.26e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; ( R ) = ( 8.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.69e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; ( R ) = ( 3.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 9.48e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0510266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667019 +Time: 3.37155e+07s, dt:197891s, Cycle: 311 +well_1Control: BHP (at the specified reference elevation): 23197054.49344515 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 6.83e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 5.28e-09 ) ; ( R ) = ( 1.16e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 4.52e-09 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.51e-02 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 6.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 3.57e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; ( R ) = ( 6.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 7.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.37e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 7.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 1.26e-11 ) ; ( R ) = ( 4.36e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0508674 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659017 +Time: 3.39134e+07s, dt:86619.3s, Cycle: 312 +well_1Control: BHP (at the specified reference elevation): 23210691.79737816 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 6.77e-08 ) ; ( R ) = ( 2.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.20e-03 ) ; ( Rwell ) = ( 7.42e-10 ) ; ( R ) = ( 8.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0235259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0294072 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.4e+07s, dt:141211s, Cycle: 313 +well_1Control: BHP (at the specified reference elevation): 23216906.115645554 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 7.05e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 4.92e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.89e-04 ) ; ( Rwell ) = ( 6.84e-12 ) ; ( R ) = ( 3.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.036329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0482442 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.39134e+07, 1.39527e+07, 1.39919e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.40842e+06, 1.48692e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.79 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.14103, 727.649 } rm^3 +compflowStatistics, reservoir: Phase mass: { 675.439, 703094 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 151.193, 211554 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 524.246, 491540 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 7.35799, 0.0675108 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 668.081, 703094 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 675.439, 0 }, { 334.02, 702754 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.38605e+07, 1.38968e+07, 1.39321e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.35546e+06, 1.42708e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.963 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.963 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215407 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64622.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150785 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215407 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23206e-08, 215407 } } kg +well_1Control: BHP (at the specified reference elevation): 23226752.29703658 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.4281 +compflowStatistics: Max component CFL number: 77.5087 +Time: 3.41412e+07s, dt:178117s, Cycle: 314 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 6.85e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 7.49e-09 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.77e-02 ) ; ( Rwell ) = ( 4.11e-09 ) ; ( R ) = ( 9.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.27e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 9.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 8.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.31e-02 ) ; ( Rwell ) = ( 2.88e-09 ) ; ( R ) = ( 8.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; ( R ) = ( 7.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.97e-04 ) ; ( Rwell ) = ( 2.59e-11 ) ; ( R ) = ( 4.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0456525 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0597886 +Time: 3.43193e+07s, dt:178117s, Cycle: 315 +well_1Control: BHP (at the specified reference elevation): 23239058.2141703 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 6.78e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 7.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 5.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.29e-02 ) ; ( Rwell ) = ( 1.35e-07 ) ; ( R ) = ( 8.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 8.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 5.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 1.35e-07 ) ; ( R ) = ( 7.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 9.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 6.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 5.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 3.24e-09 ) ; ( R ) = ( 7.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; ( R ) = ( 6.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 2.70e-09 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 6.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 9.73e-10 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 9.26e-10 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.99e-04 ) ; ( Rwell ) = ( 9.45e-12 ) ; ( R ) = ( 2.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0458388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598932 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 3.44974e+07s, dt:89058.3s, Cycle: 316 +well_1Control: BHP (at the specified reference elevation): 23251451.26020801 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 6.83e-08 ) ; ( R ) = ( 2.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 3.15e-11 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-05 ) ; ( Rwell ) = ( 2.38e-15 ) ; ( R ) = ( 1.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0240703 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0296839 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.45865e+07s, dt:144567s, Cycle: 317 +well_1Control: BHP (at the specified reference elevation): 23257840.665692605 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 7.04e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 5.39e-09 ) ; ( R ) = ( 6.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.45e-04 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 3.45e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0369835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0488254 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.47311e+07s, dt:181085s, Cycle: 318 +well_1Control: BHP (at the specified reference elevation): 23267857.21312096 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 6.79e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 7.39e-09 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.75e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 5.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 4.31e-09 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 3.87e-09 ) ; ( R ) = ( 1.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.18e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.92e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 8.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.31e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; ( R ) = ( 8.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.85e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; ( R ) = ( 7.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.33e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; ( R ) = ( 7.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 1.67e-09 ) ; ( R ) = ( 5.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.28e-04 ) ; ( Rwell ) = ( 6.88e-12 ) ; ( R ) = ( 1.28e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0462354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601441 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 3.49122e+07s, dt:87846.1s, Cycle: 319 +well_1Control: BHP (at the specified reference elevation): 23280192.90303924 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 6.68e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 6.66e-10 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-04 ) ; ( Rwell ) = ( 7.14e-12 ) ; ( R ) = ( 1.94e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0231896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0298493 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.5e+07s, dt:142235s, Cycle: 320 +well_1Control: BHP (at the specified reference elevation): 23286358.761151925 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 6.88e-08 ) ; ( R ) = ( 3.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 2.83e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.036493 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0478998 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.39488e+07, 1.3988e+07, 1.40272e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.44373e+06, 1.52221e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.816 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.19089, 727.625 } rm^3 +compflowStatistics, reservoir: Phase mass: { 693.697, 703092 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 156.384, 211568 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 537.313, 491524 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 7.8772, 0.067513 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 685.82, 703092 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 693.697, 0 }, { 345.36, 702740 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.3896e+07, 1.39322e+07, 1.39674e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.39096e+06, 1.46238e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.971 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.971 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215421 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64626.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150795 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215421 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2322e-08, 215421 } } kg +well_1Control: BHP (at the specified reference elevation): 23296242.9205968 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.43119 +compflowStatistics: Max component CFL number: 77.7876 +Time: 3.51422e+07s, dt:180153s, Cycle: 321 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 7.91e-09 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 4.02e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.51e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 8.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 7.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.83e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 7.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.60e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 6.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.69e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 6.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 5.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.41e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0458238 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606183 +Time: 3.53224e+07s, dt:180153s, Cycle: 322 +well_1Control: BHP (at the specified reference elevation): 23308639.28045349 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.09e-02 ) ; ( Rwell ) = ( 7.65e-09 ) ; ( R ) = ( 9.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 4.03e-09 ) ; ( R ) = ( 8.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; ( R ) = ( 7.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.78e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 7.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 6.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 4.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.25e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.75e-04 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 3.75e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0457735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0590396 +Time: 3.55025e+07s, dt:180153s, Cycle: 323 +well_1Control: BHP (at the specified reference elevation): 23321043.289319597 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 7.20e-09 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.84e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 4.19e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.14e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; ( R ) = ( 9.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 3.40e-09 ) ; ( R ) = ( 6.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.46e-04 ) ; ( Rwell ) = ( 3.69e-11 ) ; ( R ) = ( 8.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0456206 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0595703 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.56827e+07s, dt:200022s, Cycle: 324 +well_1Control: BHP (at the specified reference elevation): 23333323.7559468 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 6.66e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 8.62e-08 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 8.73e-08 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.73e-02 ) ; ( Rwell ) = ( 8.71e-08 ) ; ( R ) = ( 9.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.89e-02 ) ; ( Rwell ) = ( 8.68e-08 ) ; ( R ) = ( 9.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.55e-02 ) ; ( Rwell ) = ( 8.66e-08 ) ; ( R ) = ( 9.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.93e-02 ) ; ( Rwell ) = ( 8.62e-08 ) ; ( R ) = ( 8.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 8.68e-08 ) ; ( R ) = ( 6.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 8.72e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.78e-04 ) ; ( Rwell ) = ( 2.70e-11 ) ; ( R ) = ( 7.78e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0504823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0635677 +Time: 3.58827e+07s, dt:117283s, Cycle: 325 +well_1Control: BHP (at the specified reference elevation): 23346916.45004891 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 6.64e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 9.64e-10 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 5.02e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0306237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0387853 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.6e+07s, dt:166900s, Cycle: 326 +well_1Control: BHP (at the specified reference elevation): 23355132.20267334 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 6.84e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.17e-02 ) ; ( Rwell ) = ( 6.32e-09 ) ; ( R ) = ( 8.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 3.64e-09 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 9.96e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 5.94e-12 ) ; ( R ) = ( 6.22e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0422627 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055359 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.39845e+07, 1.40238e+07, 1.4063e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.47867e+06, 1.55714e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.842 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.24113, 727.601 } rm^3 +compflowStatistics, reservoir: Phase mass: { 712.223, 703091 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 161.748, 211583 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 550.475, 491508 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 8.43578, 0.0675154 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 703.787, 703091 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 712.223, 0 }, { 357.13, 702727 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.39321e+07, 1.3968e+07, 1.40032e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.4262e+06, 1.49733e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.979 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.979 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215434 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64630.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150804 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215434 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23234e-08, 215434 } } kg +well_1Control: BHP (at the specified reference elevation): 23366611.845488004 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.82736 +compflowStatistics: Max component CFL number: 90.9427 +Time: 3.61669e+07s, dt:193943s, Cycle: 327 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 6.71e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 8.84e-09 ) ; ( R ) = ( 1.99e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.94e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 6.85e-09 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.93e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; ( R ) = ( 6.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.78e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 4.16e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0487588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624885 +Time: 3.63608e+07s, dt:193943s, Cycle: 328 +well_1Control: BHP (at the specified reference elevation): 23379862.52498199 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 6.66e-08 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 8.21e-09 ) ; ( R ) = ( 1.70e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.52e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.77e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; ( R ) = ( 9.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.88e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; ( R ) = ( 7.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.24e-02 ) ; ( Rwell ) = ( 3.44e-09 ) ; ( R ) = ( 9.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 5.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.01e-04 ) ; ( Rwell ) = ( 3.31e-11 ) ; ( R ) = ( 9.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0486589 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626578 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.65548e+07s, dt:208524s, Cycle: 329 +well_1Control: BHP (at the specified reference elevation): 23393086.11976859 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 6.65e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 9.18e-09 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.45e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 5.36e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 4.86e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.30e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.22e-02 ) ; ( Rwell ) = ( 4.18e-09 ) ; ( R ) = ( 8.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 4.07e-09 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; ( R ) = ( 7.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.81e-04 ) ; ( Rwell ) = ( 7.19e-12 ) ; ( R ) = ( 5.81e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0521754 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673432 +Time: 3.67633e+07s, dt:208524s, Cycle: 330 +well_1Control: BHP (at the specified reference elevation): 23407216.850651905 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 6.60e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 9.80e-09 ) ; ( R ) = ( 1.61e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.05e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 5.50e-09 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; ( R ) = ( 7.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 3.99e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.39e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 3.88e-09 ) ; ( R ) = ( 5.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.12e-09 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 5.17e-12 ) ; ( R ) = ( 5.48e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.22e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23421332.43647807 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0520156 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661229 +Time: 3.69718e+07s, dt:28166.1s, Cycle: 331 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.35e-03 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.59e-10 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-04 ) ; ( Rwell ) = ( 2.93e-12 ) ; ( R ) = ( 1.11e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00846943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00925488 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.7e+07s, dt:56332.3s, Cycle: 332 +well_1Control: BHP (at the specified reference elevation): 23423372.594232462 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 7.05e-08 ) ; ( R ) = ( 1.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 6.84e-10 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-04 ) ; ( Rwell ) = ( 5.51e-12 ) ; ( R ) = ( 1.54e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0148161 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0180554 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 23427389.913988397 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.40154e+07, 1.40546e+07, 1.40938e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.51333e+06, 1.59178e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.865 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.2844, 727.58 } rm^3 +compflowStatistics, reservoir: Phase mass: { 728.285, 703089 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 166.393, 211595 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 561.892, 491494 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 8.91197, 0.0675175 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 719.373, 703089 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 728.285, 0 }, { 367.365, 702715 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.39631e+07, 1.39989e+07, 1.4034e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.46114e+06, 1.53199e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.986 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.986 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215446 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64633.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150812 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215446 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23247e-08, 215446 } } kg +compflowStatistics: Max phase CFL number: 0.952508 +compflowStatistics: Max component CFL number: 30.5984 +Time: 3.70563e+07s, dt:111485s, Cycle: 333 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 6.94e-08 ) ; ( R ) = ( 2.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 7.67e-10 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-03 ) ; ( Rwell ) = ( 3.74e-10 ) ; ( R ) = ( 9.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-04 ) ; ( Rwell ) = ( 4.78e-12 ) ; ( R ) = ( 1.58e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0283001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0363668 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.71678e+07s, dt:164025s, Cycle: 334 +well_1Control: BHP (at the specified reference elevation): 23435115.10840273 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 6.74e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 9.62e-08 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.34e-04 ) ; ( Rwell ) = ( 1.07e-11 ) ; ( R ) = ( 7.34e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0409617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0539138 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.73318e+07s, dt:193700s, Cycle: 335 +well_1Control: BHP (at the specified reference elevation): 23446274.05978612 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 6.61e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.42e-02 ) ; ( Rwell ) = ( 8.30e-09 ) ; ( R ) = ( 9.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 4.56e-09 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; ( R ) = ( 7.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.18e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.40e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 3.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0482437 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629037 +Time: 3.75255e+07s, dt:193700s, Cycle: 336 +well_1Control: BHP (at the specified reference elevation): 23459343.50063027 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 6.56e-08 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 7.89e-09 ) ; ( R ) = ( 1.10e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 8.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.57e-04 ) ; ( Rwell ) = ( 1.86e-11 ) ; ( R ) = ( 6.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0481335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0628997 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.77192e+07s, dt:207749s, Cycle: 337 +well_1Control: BHP (at the specified reference elevation): 23472465.82967134 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 6.58e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 9.60e-09 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 5.05e-09 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 4.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 4.47e-09 ) ; ( R ) = ( 9.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 7.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 3.49e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.75e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; ( R ) = ( 6.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; ( R ) = ( 6.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0514509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650688 +Time: 3.7927e+07s, dt:73007.5s, Cycle: 338 +well_1Control: BHP (at the specified reference elevation): 23486372.00950225 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 6.50e-08 ) ; ( R ) = ( 1.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 8.43e-10 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.94e-04 ) ; ( Rwell ) = ( 4.95e-11 ) ; ( R ) = ( 3.94e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0194029 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0233569 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.8e+07s, dt:131360s, Cycle: 339 +well_1Control: BHP (at the specified reference elevation): 23491496.011326484 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 6.81e-08 ) ; ( R ) = ( 2.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 6.88e-12 ) ; ( R ) = ( 4.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0329923 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0427688 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.40525e+07, 1.40917e+07, 1.41309e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.54792e+06, 1.62635e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.891 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.33643, 727.555 } rm^3 +compflowStatistics, reservoir: Phase mass: { 747.715, 703088 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 172.078, 211610 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 575.636, 491478 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 9.50356, 0.0675202 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 738.211, 703088 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 747.715, 0 }, { 379.721, 702701 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.40004e+07, 1.40361e+07, 1.40712e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.49589e+06, 1.56657e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.994 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.994 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215460 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64638.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150822 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215460 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23261e-08, 215460 } } kg +well_1Control: BHP (at the specified reference elevation): 23500518.74053125 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.2031 +compflowStatistics: Max component CFL number: 71.0824 +Time: 3.81314e+07s, dt:177357s, Cycle: 340 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 6.66e-08 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 6.23e-09 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 5.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.34e-02 ) ; ( Rwell ) = ( 3.81e-09 ) ; ( R ) = ( 8.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 6.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.33e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 9.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 6.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 5.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.91e-04 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 3.91e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0439382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0576282 +Time: 3.83087e+07s, dt:177357s, Cycle: 341 +well_1Control: BHP (at the specified reference elevation): 23512540.94838025 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 6.57e-08 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 6.88e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 3.57e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 3.27e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 7.34e-12 ) ; ( R ) = ( 5.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0437964 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0552192 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.84861e+07s, dt:206414s, Cycle: 342 +well_1Control: BHP (at the specified reference elevation): 23524509.061480567 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 6.54e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 8.67e-09 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.57e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; ( R ) = ( 7.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.66e-04 ) ; ( Rwell ) = ( 8.75e-12 ) ; ( R ) = ( 5.66e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0508225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664916 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.86925e+07s, dt:213549s, Cycle: 343 +well_1Control: BHP (at the specified reference elevation): 23538289.576424196 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 6.46e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 8.97e-09 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 2.11e-09 ) ; ( R ) = ( 8.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.40e-04 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 6.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0523839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681054 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.8906e+07s, dt:93961.6s, Cycle: 344 +well_1Control: BHP (at the specified reference elevation): 23552510.44683391 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 6.44e-08 ) ; ( R ) = ( 2.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 1.17e-10 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0244078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0302127 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.9e+07s, dt:151289s, Cycle: 345 +well_1Control: BHP (at the specified reference elevation): 23559044.026955284 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 6.74e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 4.55e-09 ) ; ( R ) = ( 5.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 1.75e-11 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0378342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0483339 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.40875e+07, 1.41267e+07, 1.41659e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.5822e+06, 1.66062e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.917 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.38529, 727.532 } rm^3 +compflowStatistics, reservoir: Phase mass: { 766.083, 703087 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 177.542, 211624 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 588.541, 491463 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 10.226, 0.0675227 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 755.857, 703086 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 766.083, 0 }, { 391.509, 702687 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.40356e+07, 1.40711e+07, 1.41061e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.5304e+06, 1.60085e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.002 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.002 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215474 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64642.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150832 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215474 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23275e-08, 215474 } } kg +well_1Control: BHP (at the specified reference elevation): 23569402.327994302 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.52265 +compflowStatistics: Max component CFL number: 81.5759 +Time: 3.91513e+07s, dt:190623s, Cycle: 346 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 6.62e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 7.82e-09 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.41e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 4.21e-09 ) ; ( R ) = ( 7.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 3.96e-09 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; ( R ) = ( 7.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 6.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; ( R ) = ( 4.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.47e-04 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.47e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0467914 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0587084 +Time: 3.93419e+07s, dt:190623s, Cycle: 347 +well_1Control: BHP (at the specified reference elevation): 23582253.730372503 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 6.51e-08 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 7.27e-09 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 4.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.42e-02 ) ; ( Rwell ) = ( 4.09e-09 ) ; ( R ) = ( 8.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 4.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 3.89e-09 ) ; ( R ) = ( 5.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 7.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 5.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; ( R ) = ( 6.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 5.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 4.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 9.55e-10 ) ; ( R ) = ( 4.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 8.95e-10 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 8.30e-12 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0467066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0609607 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 3.95325e+07s, dt:95311.5s, Cycle: 348 +well_1Control: BHP (at the specified reference elevation): 23595100.21441074 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 6.51e-08 ) ; ( R ) = ( 2.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.03e-04 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 8.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0241656 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0303323 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.96278e+07s, dt:153181s, Cycle: 349 +well_1Control: BHP (at the specified reference elevation): 23601626.873685278 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 6.62e-08 ) ; ( R ) = ( 3.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.44e-04 ) ; ( Rwell ) = ( 1.03e-11 ) ; ( R ) = ( 4.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0374395 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0495068 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.9781e+07s, dt:190329s, Cycle: 350 +well_1Control: BHP (at the specified reference elevation): 23611846.41018417 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 6.44e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 7.35e-09 ) ; ( R ) = ( 1.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 4.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.11e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; ( R ) = ( 8.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.05e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 8.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 7.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; ( R ) = ( 5.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 6.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 6.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 5.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 9.05e-10 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 7.89e-10 ) ; ( R ) = ( 4.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 7.12e-10 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 2.87e-04 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 2.87e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23624503.087347593 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0464124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606752 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 3.99714e+07s, dt:28643.3s, Cycle: 351 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 6.41e-08 ) ; ( R ) = ( 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-03 ) ; ( Rwell ) = ( 1.48e-10 ) ; ( R ) = ( 5.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-04 ) ; ( Rwell ) = ( 2.29e-12 ) ; ( R ) = ( 1.06e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.77e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23626519.15474152 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00812824 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00910817 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4e+07s, dt:57286.7s, Cycle: 352 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 6.78e-08 ) ; ( R ) = ( 1.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 6.86e-10 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-04 ) ; ( Rwell ) = ( 3.41e-12 ) ; ( R ) = ( 2.08e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0146458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0185954 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.41185e+07, 1.41577e+07, 1.41969e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.61642e+06, 1.69483e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.939 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.42866, 727.511 } rm^3 +compflowStatistics, reservoir: Phase mass: { 782.486, 703085 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 182.365, 211636 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 600.121, 491449 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 10.7324, 0.067525 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 771.754, 703085 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 782.486, 0 }, { 401.894, 702676 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.40667e+07, 1.41022e+07, 1.41371e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.56475e+06, 1.63508e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.009 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.009 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215485 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64645.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150840 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215485 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23287e-08, 215485 } } kg +well_1Control: BHP (at the specified reference elevation): 23630520.78997274 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.952863 +compflowStatistics: Max component CFL number: 30.7924 +Time: 4.00573e+07s, dt:112232s, Cycle: 353 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-05 ) ; ( Rwell ) = ( 8.93e-15 ) ; ( R ) = ( 1.75e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0278209 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0359435 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.01695e+07s, dt:166108s, Cycle: 354 +well_1Control: BHP (at the specified reference elevation): 23638188.74484022 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 6.58e-08 ) ; ( R ) = ( 3.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 4.89e-09 ) ; ( R ) = ( 6.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.32e-04 ) ; ( Rwell ) = ( 5.23e-12 ) ; ( R ) = ( 3.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0404657 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0536024 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.03356e+07s, dt:196850s, Cycle: 355 +well_1Control: BHP (at the specified reference elevation): 23649219.750720732 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 6.40e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 7.34e-09 ) ; ( R ) = ( 1.92e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.57e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 5.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 5.84e-09 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 4.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 4.18e-09 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 4.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 3.44e-09 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.87e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.87e-02 ) ; ( Rwell ) = ( 3.03e-09 ) ; ( R ) = ( 9.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.34e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 9.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.42e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 8.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.03e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 8.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.84e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 7.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 7.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.53e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.41e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 7.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 6.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.25e-04 ) ; ( Rwell ) = ( 1.29e-11 ) ; ( R ) = ( 2.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0478467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0620653 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.05325e+07s, dt:98425s, Cycle: 356 +well_1Control: BHP (at the specified reference elevation): 23662281.87871977 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 2.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 6.10e-11 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-05 ) ; ( Rwell ) = ( 1.29e-14 ) ; ( R ) = ( 2.19e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0248353 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0318734 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.06309e+07s, dt:154540s, Cycle: 357 +well_1Control: BHP (at the specified reference elevation): 23668994.657031752 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 6.56e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 4.94e-09 ) ; ( R ) = ( 5.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.34e-04 ) ; ( Rwell ) = ( 7.61e-12 ) ; ( R ) = ( 5.34e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.037593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0497236 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.07854e+07s, dt:191525s, Cycle: 358 +well_1Control: BHP (at the specified reference elevation): 23679356.747060962 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 6.45e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.58e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 3.81e-09 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 3.13e-09 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.44e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.46e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 9.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.53e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 9.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.28e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.55e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 2.32e-11 ) ; ( R ) = ( 8.02e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0463729 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0611541 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.0977e+07s, dt:23033.1s, Cycle: 359 +well_1Control: BHP (at the specified reference elevation): 23692087.686563976 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-03 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 8.72e-11 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.28e-05 ) ; ( Rwell ) = ( 2.30e-12 ) ; ( R ) = ( 7.28e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00672766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00738499 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.1e+07s, dt:46066.2s, Cycle: 360 +well_1Control: BHP (at the specified reference elevation): 23693715.40838561 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 6.79e-08 ) ; ( R ) = ( 1.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.03e-03 ) ; ( Rwell ) = ( 3.16e-10 ) ; ( R ) = ( 9.03e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-04 ) ; ( Rwell ) = ( 1.12e-11 ) ; ( R ) = ( 1.17e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0117717 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0147002 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +well_1Control: BHP (at the specified reference elevation): 23696935.57147196 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.41521e+07, 1.41914e+07, 1.42305e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.6505e+06, 1.72889e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.964 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.47573, 727.488 } rm^3 +compflowStatistics, reservoir: Phase mass: { 800.391, 703084 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 187.696, 211649 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 612.695, 491435 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 11.3673, 0.0675276 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 789.023, 703084 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 800.391, 0 }, { 413.225, 702663 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.41005e+07, 1.41359e+07, 1.41708e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.59896e+06, 1.66915e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.016 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.016 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215498 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64649.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150849 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215498 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.233e-08, 215498 } } kg +compflowStatistics: Max phase CFL number: 0.763239 +compflowStatistics: Max component CFL number: 24.677 +Time: 4.10461e+07s, dt:92132.3s, Cycle: 361 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 6.72e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.46e-04 ) ; ( Rwell ) = ( 6.90e-12 ) ; ( R ) = ( 6.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.022642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0296684 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.11382e+07s, dt:149592s, Cycle: 362 +well_1Control: BHP (at the specified reference elevation): 23703180.044994958 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 6.51e-08 ) ; ( R ) = ( 3.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 4.36e-09 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.74e-04 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 2.74e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.036185 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.048301 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.12878e+07s, dt:188559s, Cycle: 363 +well_1Control: BHP (at the specified reference elevation): 23713028.123583935 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 6.32e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 6.68e-09 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 3.53e-09 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; ( R ) = ( 5.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.56e-09 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 5.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 9.65e-10 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.32e-04 ) ; ( Rwell ) = ( 1.21e-11 ) ; ( R ) = ( 1.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0454834 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0591959 +Time: 4.14764e+07s, dt:188559s, Cycle: 364 +well_1Control: BHP (at the specified reference elevation): 23725387.2809911 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 6.29e-08 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 3.08e-08 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 4.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.78e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 7.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; ( R ) = ( 7.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; ( R ) = ( 7.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; ( R ) = ( 7.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; ( R ) = ( 6.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.30e-04 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 2.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0456477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0597867 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.16649e+07s, dt:94279.7s, Cycle: 365 +well_1Control: BHP (at the specified reference elevation): 23737942.179643117 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 6.38e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.04e-04 ) ; ( Rwell ) = ( 1.01e-10 ) ; ( R ) = ( 5.04e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.71e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23744395.319422804 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0237649 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0297912 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.17592e+07s, dt:152789s, Cycle: 366 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 6.57e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-04 ) ; ( Rwell ) = ( 8.25e-12 ) ; ( R ) = ( 2.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23754587.9673087 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0367423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.04846 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.1912e+07s, dt:88022.2s, Cycle: 367 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 1.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 8.77e-10 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.44e-04 ) ; ( Rwell ) = ( 9.47e-11 ) ; ( R ) = ( 7.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0219031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0279376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.2e+07s, dt:146849s, Cycle: 368 +well_1Control: BHP (at the specified reference elevation): 23760559.06556952 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 6.51e-08 ) ; ( R ) = ( 3.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.64e-04 ) ; ( Rwell ) = ( 7.03e-12 ) ; ( R ) = ( 2.64e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0352525 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0471043 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.41893e+07, 1.42285e+07, 1.42677e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.68438e+06, 1.76276e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 729.991 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.52752, 727.463 } rm^3 +compflowStatistics, reservoir: Phase mass: { 820.218, 703083 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 193.555, 211664 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 626.663, 491419 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 11.9323, 0.0675305 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 808.286, 703083 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 820.218, 0 }, { 425.944, 702649 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.41379e+07, 1.41732e+07, 1.42079e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.63297e+06, 1.70303e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.025 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.025 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215512 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64653.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150859 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215512 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23315e-08, 215512 } } kg +well_1Control: BHP (at the specified reference elevation): 23770246.576590527 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.40474 +compflowStatistics: Max component CFL number: 78.3709 +Time: 4.21468e+07s, dt:187800s, Cycle: 369 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 6.32e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 6.67e-09 ) ; ( R ) = ( 1.93e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.63e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 5.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 4.79e-09 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 4.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.46e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.40e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 9.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; ( R ) = ( 8.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.20e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; ( R ) = ( 8.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 7.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 6.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.37e-04 ) ; ( Rwell ) = ( 9.95e-12 ) ; ( R ) = ( 6.37e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.50e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23782545.661265466 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0449761 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0579621 +Time: 4.23346e+07s, dt:187800s, Cycle: 370 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; ( R ) = ( 8.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 7.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; ( R ) = ( 6.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 2.01e-09 ) ; ( R ) = ( 6.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 5.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.46e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 2.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0448393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594175 +Time: 4.25224e+07s, dt:187800s, Cycle: 371 +well_1Control: BHP (at the specified reference elevation): 23794879.814696297 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 6.28e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 6.22e-09 ) ; ( R ) = ( 1.47e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 3.68e-09 ) ; ( R ) = ( 8.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.74e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 7.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 7.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 6.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 9.77e-10 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 8.93e-10 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 8.22e-10 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 5.44e-12 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0447083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0589015 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.27102e+07s, dt:93899.9s, Cycle: 372 +well_1Control: BHP (at the specified reference elevation): 23807226.48757747 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 6.28e-08 ) ; ( R ) = ( 2.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 8.48e-10 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 7.33e-10 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.92e-04 ) ; ( Rwell ) = ( 3.20e-12 ) ; ( R ) = ( 2.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0233475 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0294276 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.28041e+07s, dt:153032s, Cycle: 373 +well_1Control: BHP (at the specified reference elevation): 23813589.834803715 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 6.48e-08 ) ; ( R ) = ( 3.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; ( R ) = ( 3.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.65e-04 ) ; ( Rwell ) = ( 1.24e-11 ) ; ( R ) = ( 1.65e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0363665 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0480917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.29572e+07s, dt:42819.8s, Cycle: 374 +well_1Control: BHP (at the specified reference elevation): 23823698.93242729 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-03 ) ; ( Rwell ) = ( 6.31e-08 ) ; ( R ) = ( 9.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 1.87e-10 ) ; ( R ) = ( 7.95e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 3.66e-11 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0111762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0136664 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.3e+07s, dt:85639.6s, Cycle: 375 +well_1Control: BHP (at the specified reference elevation): 23826633.257579908 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 6.55e-08 ) ; ( R ) = ( 1.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 5.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.020834 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.026932 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.42208e+07, 1.426e+07, 1.42992e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.71786e+06, 1.79623e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.014 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.57129, 727.443 } rm^3 +compflowStatistics, reservoir: Phase mass: { 837.089, 703082 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 198.63, 211677 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 638.459, 491405 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 12.6649, 0.067533 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 824.424, 703082 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 837.089, 0 }, { 436.831, 702637 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.41696e+07, 1.42047e+07, 1.42394e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.66673e+06, 1.73651e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.032 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.032 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215524 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64657.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150867 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215524 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23327e-08, 215524 } } kg +well_1Control: BHP (at the specified reference elevation): 23832409.69375386 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.40028 +compflowStatistics: Max component CFL number: 45.5599 +Time: 4.30856e+07s, dt:145194s, Cycle: 376 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 6.44e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 9.95e-08 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 7.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.51e-04 ) ; ( Rwell ) = ( 5.98e-12 ) ; ( R ) = ( 3.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0346864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0461165 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.32308e+07s, dt:187944s, Cycle: 377 +well_1Control: BHP (at the specified reference elevation): 23842004.224495083 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 6.31e-08 ) ; ( R ) = ( 4.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 6.22e-09 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 3.57e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.80e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 9.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.45e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; ( R ) = ( 7.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 2.15e-09 ) ; ( R ) = ( 7.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 5.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.13e-04 ) ; ( Rwell ) = ( 5.10e-12 ) ; ( R ) = ( 3.13e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0445948 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059377 +Time: 4.34188e+07s, dt:187944s, Cycle: 378 +well_1Control: BHP (at the specified reference elevation): 23854211.301490806 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.84e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.98e-02 ) ; ( Rwell ) = ( 3.58e-09 ) ; ( R ) = ( 8.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.63e-02 ) ; ( Rwell ) = ( 2.79e-09 ) ; ( R ) = ( 8.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.49e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 8.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 2.37e-09 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.53e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 7.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 2.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.01e-04 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 3.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0444601 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585409 +Time: 4.36067e+07s, dt:187944s, Cycle: 379 +well_1Control: BHP (at the specified reference elevation): 23866446.167995274 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 6.21e-08 ) ; ( R ) = ( 4.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 5.60e-09 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.07e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 9.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.96e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 7.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.53e-02 ) ; ( Rwell ) = ( 2.46e-09 ) ; ( R ) = ( 6.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 4.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0443223 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585533 +Time: 4.37947e+07s, dt:187944s, Cycle: 380 +well_1Control: BHP (at the specified reference elevation): 23878704.436387382 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 6.22e-08 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.06e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; ( R ) = ( 8.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.06e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; ( R ) = ( 7.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 2.32e-09 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.09e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.45e-04 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.45e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0441857 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0573088 +Time: 4.39826e+07s, dt:17390.2s, Cycle: 381 +well_1Control: BHP (at the specified reference elevation): 23890913.427012768 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.72e-03 ) ; ( Rwell ) = ( 6.19e-08 ) ; ( R ) = ( 3.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-03 ) ; ( Rwell ) = ( 4.14e-11 ) ; ( R ) = ( 3.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 1.27e-11 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.26e-06 ) ; ( Rwell ) = ( 7.52e-14 ) ; ( R ) = ( 5.26e-06 ) ; + Last LinSolve(iter,res) = ( 7, 8.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00500373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00526835 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.4e+07s, dt:34780.4s, Cycle: 382 +well_1Control: BHP (at the specified reference elevation): 23892100.63856961 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 6.50e-08 ) ; ( R ) = ( 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 1.83e-10 ) ; ( R ) = ( 6.73e-03 ) ; + Last LinSolve(iter,res) = ( 3, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-04 ) ; ( Rwell ) = ( 3.14e-12 ) ; ( R ) = ( 1.09e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00872174 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0106634 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.42522e+07, 1.42915e+07, 1.43306e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.75102e+06, 1.82938e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.037 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.61473, 727.422 } rm^3 +compflowStatistics, reservoir: Phase mass: { 853.939, 703082 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 203.687, 211689 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 650.252, 491392 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 13.264, 0.0675356 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 840.675, 703082 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 853.939, 0 }, { 448.043, 702625 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.42014e+07, 1.42362e+07, 1.42709e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.70027e+06, 1.76967e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.039 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.039 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215536 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64660.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150875 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215536 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.2334e-08, 215536 } } kg +well_1Control: BHP (at the specified reference elevation): 23894476.892855093 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.560971 +compflowStatistics: Max component CFL number: 18.4448 +Time: 4.40348e+07s, dt:69560.9s, Cycle: 383 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 6.50e-08 ) ; ( R ) = ( 1.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 9.23e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.33e-04 ) ; ( Rwell ) = ( 2.11e-12 ) ; ( R ) = ( 3.33e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0169628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0218771 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.41043e+07s, dt:128415s, Cycle: 384 +well_1Control: BHP (at the specified reference elevation): 23899162.93406924 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 6.41e-08 ) ; ( R ) = ( 2.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 9.35e-12 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 3.60e-15 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.82e-04 ) ; +well_1Control: BHP (at the specified reference elevation): 23907639.87774355 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0305748 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.03988 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.42328e+07s, dt:180070s, Cycle: 385 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 6.28e-08 ) ; ( R ) = ( 3.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 5.19e-09 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.09e-02 ) ; ( Rwell ) = ( 3.17e-09 ) ; ( R ) = ( 9.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.53e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; ( R ) = ( 6.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 2.21e-09 ) ; ( R ) = ( 7.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.73e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 6.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.76e-04 ) ; ( Rwell ) = ( 4.51e-12 ) ; ( R ) = ( 6.76e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0422762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.05654 +Time: 4.44128e+07s, dt:180070s, Cycle: 386 +well_1Control: BHP (at the specified reference elevation): 23919375.357282043 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 5.25e-09 ) ; ( R ) = ( 1.28e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.99e-02 ) ; ( Rwell ) = ( 3.28e-09 ) ; ( R ) = ( 7.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.45e-02 ) ; ( Rwell ) = ( 2.73e-09 ) ; ( R ) = ( 7.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 6.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 6.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 6.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 5.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 5.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 9.78e-10 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 8.34e-10 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 7.76e-10 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.11e-04 ) ; ( Rwell ) = ( 9.54e-12 ) ; ( R ) = ( 2.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0422662 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0554777 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.45929e+07s, dt:90034.8s, Cycle: 387 +well_1Control: BHP (at the specified reference elevation): 23931124.434155077 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 1.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.84e-03 ) ; ( Rwell ) = ( 5.11e-10 ) ; ( R ) = ( 8.84e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.96e-04 ) ; ( Rwell ) = ( 7.26e-12 ) ; ( R ) = ( 1.96e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0220389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0282 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.46829e+07s, dt:149583s, Cycle: 388 +well_1Control: BHP (at the specified reference elevation): 23937165.554262083 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 6.37e-08 ) ; ( R ) = ( 3.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 9.80e-10 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-04 ) ; ( Rwell ) = ( 2.51e-11 ) ; ( R ) = ( 3.08e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0351492 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0466144 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.48325e+07s, dt:167486s, Cycle: 389 +well_1Control: BHP (at the specified reference elevation): 23946970.378617093 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 6.23e-08 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 4.75e-09 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.60e-04 ) ; ( Rwell ) = ( 2.04e-11 ) ; ( R ) = ( 4.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0391782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0523059 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.5e+07s, dt:201430s, Cycle: 390 +well_1Control: BHP (at the specified reference elevation): 23957777.523177348 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 6.58e-09 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.39e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.54e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 9.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.29e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; ( R ) = ( 8.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 6.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; ( R ) = ( 7.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 1.58e-09 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; ( R ) = ( 5.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.39e-04 ) ; ( Rwell ) = ( 1.74e-11 ) ; ( R ) = ( 2.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0469573 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0622768 +compflowStatistics, reservoir: Pressure (min, average, max): 1.42908e+07, 1.433e+07, 1.43692e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.78428e+06, 1.86263e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.065 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.66811, 727.397 } rm^3 +compflowStatistics, reservoir: Phase mass: { 874.762, 703081 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 210.028, 211705 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 664.734, 491376 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 14.0215, 0.0675387 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 860.74, 703081 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 874.762, 0 }, { 461.715, 702610 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.42403e+07, 1.4275e+07, 1.43095e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.7336e+06, 1.80293e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.047 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.047 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215551 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64665.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150886 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215551 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23355e-08, 215551 } } kg +well_1Control: BHP (at the specified reference elevation): 23970683.78202282 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 3.20722 +compflowStatistics: Max component CFL number: 106.411 +Time: 4.52014e+07s, dt:201430s, Cycle: 391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 6.08e-08 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 6.67e-09 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.95e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 3.75e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.78e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 9.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.22e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 9.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 9.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 8.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 2.04e-09 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.11e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 8.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.71e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 7.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.76e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.33e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 7.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.10e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 7.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 2.97e-04 ) ; ( Rwell ) = ( 4.36e-12 ) ; ( R ) = ( 2.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.04705 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613645 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.54029e+07s, dt:100715s, Cycle: 392 +well_1Control: BHP (at the specified reference elevation): 23983724.644721027 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 6.14e-08 ) ; ( R ) = ( 2.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.14e-04 ) ; ( Rwell ) = ( 9.76e-11 ) ; ( R ) = ( 6.14e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.024691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0306484 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.55036e+07s, dt:161087s, Cycle: 393 +well_1Control: BHP (at the specified reference elevation): 23990486.883023918 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 6.37e-08 ) ; ( R ) = ( 3.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 4.76e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-04 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 3.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0375718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0497155 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.56647e+07s, dt:199658s, Cycle: 394 +well_1Control: BHP (at the specified reference elevation): 24001008.839580745 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 6.19e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 6.39e-09 ) ; ( R ) = ( 1.89e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.44e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 5.10e-09 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 4.00e-09 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.99e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; ( R ) = ( 8.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.52e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 8.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.78e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 8.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.69e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 7.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 7.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 5.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.65e-04 ) ; ( Rwell ) = ( 1.10e-11 ) ; ( R ) = ( 6.65e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0462788 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568539 +Time: 4.58643e+07s, dt:135681s, Cycle: 395 +well_1Control: BHP (at the specified reference elevation): 24013858.17743613 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 6.09e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 9.32e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 5.19e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 4.68e-10 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.64e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.09e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 9.75e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 3.64e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 9.13e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.23e-10 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.94e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 2.62e-10 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.56e-05 ) ; ( Rwell ) = ( 1.35e-12 ) ; ( R ) = ( 5.56e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0319671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0402889 +Time: 4.6e+07s, dt:135681s, Cycle: 396 +well_1Control: BHP (at the specified reference elevation): 24022742.80697277 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 8.81e-10 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 7.73e-10 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 6.62e-10 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 5.68e-10 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 5.08e-10 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 4.64e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.63e-05 ) ; ( Rwell ) = ( 2.20e-11 ) ; ( R ) = ( 8.63e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24031633.374319736 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0320495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0414695 +compflowStatistics, reservoir: Pressure (min, average, max): 1.43217e+07, 1.43609e+07, 1.44e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.81716e+06, 1.8955e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.087 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.71078, 727.376 } rm^3 +compflowStatistics, reservoir: Phase mass: { 891.511, 703080 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 215.152, 211717 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 676.359, 491363 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 14.7685, 0.0675413 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 876.742, 703080 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 891.511, 0 }, { 472.589, 702598 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.42712e+07, 1.43058e+07, 1.43403e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.76668e+06, 1.83582e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.054 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.054 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215563 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64668.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150894 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215563 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23368e-08, 215563 } } kg +compflowStatistics: Max phase CFL number: 2.16833 +compflowStatistics: Max component CFL number: 71.457 +Time: 4.61357e+07s, dt:135681s, Cycle: 397 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 6.20e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 8.52e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-04 ) ; ( Rwell ) = ( 4.78e-12 ) ; ( R ) = ( 2.80e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24040480.77025289 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0317823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0417677 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.62714e+07s, dt:185579s, Cycle: 398 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 6.16e-08 ) ; ( R ) = ( 3.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 5.35e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 4.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 6.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 2.81e-09 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.35e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 9.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 5.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 1.55e-09 ) ; ( R ) = ( 5.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 4.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 9.79e-10 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 8.39e-10 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 1.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 7.95e-10 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 8.09e-05 ) ; ( Rwell ) = ( 5.75e-12 ) ; ( R ) = ( 8.09e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0428866 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561974 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.64569e+07s, dt:92789.4s, Cycle: 399 +well_1Control: BHP (at the specified reference elevation): 24052418.484955132 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 6.08e-08 ) ; ( R ) = ( 1.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.33e-03 ) ; ( Rwell ) = ( 4.70e-10 ) ; ( R ) = ( 8.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 6.18e-12 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0222991 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0286909 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.65497e+07s, dt:152971s, Cycle: 400 +well_1Control: BHP (at the specified reference elevation): 24058547.06041737 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 6.24e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.06e-04 ) ; ( Rwell ) = ( 9.65e-12 ) ; ( R ) = ( 4.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0353673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0460247 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.67027e+07s, dt:198236s, Cycle: 401 +well_1Control: BHP (at the specified reference elevation): 24068460.967796862 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 6.12e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 5.92e-09 ) ; ( R ) = ( 1.76e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 4.72e-09 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 3.83e-09 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.73e-02 ) ; ( Rwell ) = ( 3.14e-09 ) ; ( R ) = ( 9.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.06e-02 ) ; ( Rwell ) = ( 2.71e-09 ) ; ( R ) = ( 7.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 6.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 7.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.24e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 7.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.55e-04 ) ; ( Rwell ) = ( 1.02e-11 ) ; ( R ) = ( 2.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.04567 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588434 +Time: 4.69009e+07s, dt:99063.6s, Cycle: 402 +well_1Control: BHP (at the specified reference elevation): 24081171.143941823 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 2.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 7.49e-10 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.58e-04 ) ; ( Rwell ) = ( 1.61e-10 ) ; ( R ) = ( 4.58e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0237131 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0305382 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.7e+07s, dt:158712s, Cycle: 403 +well_1Control: BHP (at the specified reference elevation): 24087686.39728591 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 6.22e-08 ) ; ( R ) = ( 3.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 3.06e-12 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0364896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0483924 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.43552e+07, 1.43944e+07, 1.44335e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.85002e+06, 1.92836e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.111 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.75703, 727.354 } rm^3 +compflowStatistics, reservoir: Phase mass: { 909.771, 703080 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 220.722, 211731 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 689.049, 491349 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 15.6143, 0.0675441 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 894.157, 703080 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 909.771, 0 }, { 484.577, 702586 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.43049e+07, 1.43394e+07, 1.43738e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.79965e+06, 1.86868e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.062 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.062 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215575 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64672.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150903 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215575 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.23437e-08, 215575 } } kg +well_1Control: BHP (at the specified reference elevation): 24097872.314797457 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.51574 +compflowStatistics: Max component CFL number: 83.3084 +Time: 4.71587e+07s, dt:199835s, Cycle: 404 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 6.87e-09 ) ; ( R ) = ( 1.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 3.56e-09 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 6.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.06e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; ( R ) = ( 8.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.24e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 8.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 7.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.65e-04 ) ; ( Rwell ) = ( 1.11e-11 ) ; ( R ) = ( 1.65e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0457965 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575048 +Time: 4.73585e+07s, dt:199835s, Cycle: 405 +well_1Control: BHP (at the specified reference elevation): 24110502.861199938 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 5.96e-08 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 5.87e-09 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.49e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 9.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.21e-02 ) ; ( Rwell ) = ( 2.78e-09 ) ; ( R ) = ( 9.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 7.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 7.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 1.91e-09 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 6.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 7.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 5.48e-12 ) ; ( R ) = ( 5.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0458774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0596343 +Time: 4.75584e+07s, dt:199835s, Cycle: 406 +well_1Control: BHP (at the specified reference elevation): 24123334.355944887 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 6.44e-08 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 6.47e-08 ) ; ( R ) = ( 8.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 6.49e-08 ) ; ( R ) = ( 7.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 6.48e-08 ) ; ( R ) = ( 8.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 6.47e-08 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 6.54e-08 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 6.50e-08 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 6.53e-08 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 1.41e-11 ) ; ( R ) = ( 4.68e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0457857 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0592362 +Time: 4.77582e+07s, dt:199835s, Cycle: 407 +well_1Control: BHP (at the specified reference elevation): 24136185.188354984 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 5.85e-09 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 4.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.09e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; ( R ) = ( 9.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.61e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 8.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.42e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 9.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; ( R ) = ( 7.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.27e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 7.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 7.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 6.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.25e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.28e-04 ) ; ( Rwell ) = ( 1.94e-11 ) ; ( R ) = ( 3.28e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.045764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593045 +Time: 4.79581e+07s, dt:41947.4s, Cycle: 408 +well_1Control: BHP (at the specified reference elevation): 24149047.187782727 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.66e-03 ) ; ( Rwell ) = ( 6.06e-08 ) ; ( R ) = ( 8.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 2.36e-10 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 8.61e-12 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.010621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0127747 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 4.8e+07s, dt:83894.9s, Cycle: 409 +well_1Control: BHP (at the specified reference elevation): 24151853.848517496 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 6.29e-08 ) ; ( R ) = ( 1.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-04 ) ; ( Rwell ) = ( 6.71e-12 ) ; ( R ) = ( 3.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0195998 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0252683 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.43853e+07, 1.44245e+07, 1.44636e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.88249e+06, 1.96081e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.133 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.79841, 727.335 } rm^3 +compflowStatistics, reservoir: Phase mass: { 926.209, 703079 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 225.813, 211743 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 700.396, 491337 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 16.2406, 0.0675466 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 909.969, 703079 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 926.209, 0 }, { 495.493, 702574 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.43351e+07, 1.43695e+07, 1.44039e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.83237e+06, 1.90114e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.068 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.068 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215587 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64676.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150911 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215587 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.29453e-08, 215587 } } kg +well_1Control: BHP (at the specified reference elevation): 24157371.80898827 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.33027 +compflowStatistics: Max component CFL number: 43.9054 +Time: 4.80839e+07s, dt:146162s, Cycle: 410 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 6.19e-08 ) ; ( R ) = ( 3.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 3.63e-09 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 8.12e-10 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.93e-04 ) ; ( Rwell ) = ( 8.19e-12 ) ; ( R ) = ( 3.93e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0333576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0432376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.82301e+07s, dt:196160s, Cycle: 411 +well_1Control: BHP (at the specified reference elevation): 24166737.97122619 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 6.02e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 2.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 4.59e-09 ) ; ( R ) = ( 1.61e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.30e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 4.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 4.01e-09 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.85e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; ( R ) = ( 9.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.11e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.69e-02 ) ; ( Rwell ) = ( 2.76e-09 ) ; ( R ) = ( 8.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.45e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 7.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 6.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 4.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.87e-04 ) ; ( Rwell ) = ( 9.03e-12 ) ; ( R ) = ( 4.87e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0445917 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0592659 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.84262e+07s, dt:98079.8s, Cycle: 412 +well_1Control: BHP (at the specified reference elevation): 24179116.62856215 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 5.93e-08 ) ; ( R ) = ( 2.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 5.28e-10 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 2.14e-10 ) ; ( R ) = ( 6.67e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24185509.4617766 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0231644 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0295619 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.85243e+07s, dt:159512s, Cycle: 413 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 6.14e-08 ) ; ( R ) = ( 3.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.85e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 9.71e-10 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 8.98e-10 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 4.32e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0361895 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0471985 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.86838e+07s, dt:203759s, Cycle: 414 +well_1Control: BHP (at the specified reference elevation): 24195713.377336256 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 6.01e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 5.67e-09 ) ; ( R ) = ( 1.60e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.98e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 7.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.75e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 6.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 6.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 6.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 7.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.49e-04 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 4.49e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0461782 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606834 +Time: 4.88876e+07s, dt:112432s, Cycle: 415 +well_1Control: BHP (at the specified reference elevation): 24208722.0231421 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 2.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 5.01e-11 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-05 ) ; ( Rwell ) = ( 2.50e-15 ) ; ( R ) = ( 1.63e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0264674 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0337015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.9e+07s, dt:171836s, Cycle: 416 +well_1Control: BHP (at the specified reference elevation): 24216067.23512858 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 6.13e-08 ) ; ( R ) = ( 3.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 4.33e-09 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 4.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.26e-02 ) ; ( Rwell ) = ( 2.59e-09 ) ; ( R ) = ( 7.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 4.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 2.26e-09 ) ; ( R ) = ( 7.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 5.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 9.47e-10 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.86e-04 ) ; ( Rwell ) = ( 1.28e-11 ) ; ( R ) = ( 2.86e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0388892 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0519342 +compflowStatistics, reservoir: Pressure (min, average, max): 1.44205e+07, 1.44597e+07, 1.44988e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.91496e+06, 1.99328e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.159 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.84684, 727.312 } rm^3 +compflowStatistics, reservoir: Phase mass: { 945.55, 703079 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 231.815, 211757 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 713.735, 491322 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 17.0644, 0.0675497 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 928.486, 703079 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 945.55, 0 }, { 508.32, 702561 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.43705e+07, 1.44048e+07, 1.44392e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.86494e+06, 1.93362e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.076 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.076 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215600 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64680.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150920 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215600 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 1.13364e-07, 215600 } } kg +well_1Control: BHP (at the specified reference elevation): 24227032.600326665 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.69897 +compflowStatistics: Max component CFL number: 89.6155 +Time: 4.91718e+07s, dt:171836s, Cycle: 417 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 3.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 9.33e-08 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 4.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 7.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 4.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 6.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 6.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 9.27e-10 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 8.28e-10 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 7.84e-10 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.17e-04 ) ; ( Rwell ) = ( 7.91e-12 ) ; ( R ) = ( 5.17e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0388337 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051742 +Time: 4.93437e+07s, dt:171836s, Cycle: 418 +well_1Control: BHP (at the specified reference elevation): 24237921.46073548 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.06e-02 ) ; ( Rwell ) = ( 4.10e-09 ) ; ( R ) = ( 9.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 2.34e-09 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 2.07e-09 ) ; ( R ) = ( 5.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 5.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.54e-09 ) ; ( R ) = ( 5.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 4.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 9.72e-10 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 8.41e-10 ) ; ( R ) = ( 4.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 7.29e-10 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 7.23e-10 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 6.31e-10 ) ; ( R ) = ( 3.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 5.60e-10 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 9.11e-05 ) ; ( Rwell ) = ( 6.33e-12 ) ; ( R ) = ( 9.11e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0388612 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518838 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 4.95155e+07s, dt:85917.8s, Cycle: 419 +well_1Control: BHP (at the specified reference elevation): 24248846.415536605 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 1.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.79e-10 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 9.49e-11 ) ; ( R ) = ( 4.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.28e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24254428.48428713 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0201536 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0245737 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.96014e+07s, dt:151432s, Cycle: 420 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 6.09e-08 ) ; ( R ) = ( 3.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 3.58e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 9.02e-10 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-04 ) ; ( Rwell ) = ( 6.94e-12 ) ; ( R ) = ( 1.77e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0341091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0457231 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.97529e+07s, dt:196974s, Cycle: 421 +well_1Control: BHP (at the specified reference elevation): 24264062.319026485 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 4.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 5.44e-09 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.57e-02 ) ; ( Rwell ) = ( 3.26e-09 ) ; ( R ) = ( 9.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; ( R ) = ( 9.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.38e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 8.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.03e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 8.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 7.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 7.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.47e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 7.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 6.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 6.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.56e-04 ) ; ( Rwell ) = ( 1.60e-11 ) ; ( R ) = ( 6.56e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0443029 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0569691 +Time: 4.99498e+07s, dt:50168.6s, Cycle: 422 +well_1Control: BHP (at the specified reference elevation): 24276576.39663088 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 1.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 3.70e-10 ) ; ( R ) = ( 9.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-04 ) ; ( Rwell ) = ( 4.42e-12 ) ; ( R ) = ( 1.68e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0126344 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0148912 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5e+07s, dt:100337s, Cycle: 423 +well_1Control: BHP (at the specified reference elevation): 24279932.141187843 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 6.25e-08 ) ; ( R ) = ( 2.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.22e-05 ) ; ( Rwell ) = ( 1.64e-15 ) ; ( R ) = ( 2.22e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0230685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0306683 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.44506e+07, 1.44898e+07, 1.45289e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.94725e+06, 2.02556e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.181 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.8882, 727.293 } rm^3 +compflowStatistics, reservoir: Phase mass: { 962.16, 703079 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 237.032, 211769 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 725.128, 491310 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 17.8699, 0.0675523 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 944.29, 703079 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 962.16, 0 }, { 519.163, 702549 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.44006e+07, 1.44348e+07, 1.44692e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.89737e+06, 1.96591e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.083 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.083 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215612 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64683.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150928 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215612 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 4.83548e-06, 215612 } } kg +well_1Control: BHP (at the specified reference elevation): 24286489.51832164 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.58032 +compflowStatistics: Max component CFL number: 52.1728 +Time: 5.01003e+07s, dt:160434s, Cycle: 424 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 6.11e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 6.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 9.87e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-04 ) ; ( Rwell ) = ( 1.88e-11 ) ; ( R ) = ( 1.95e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0362028 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0486202 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.02608e+07s, dt:201453s, Cycle: 425 +well_1Control: BHP (at the specified reference elevation): 24296708.221128188 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 5.28e-09 ) ; ( R ) = ( 1.76e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 4.65e-09 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.16e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 9.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 9.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; ( R ) = ( 8.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.75e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 6.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.62e-04 ) ; ( Rwell ) = ( 8.08e-12 ) ; ( R ) = ( 3.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24309387.253467396 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0452726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599782 +Time: 5.04622e+07s, dt:201453s, Cycle: 426 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 5.49e-09 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.64e-02 ) ; ( Rwell ) = ( 3.13e-09 ) ; ( R ) = ( 9.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 8.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 2.49e-09 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 8.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.37e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; ( R ) = ( 8.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.81e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 7.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 7.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 7.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 1.18e-09 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 9.18e-10 ) ; ( R ) = ( 5.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 8.39e-10 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.42e-04 ) ; ( Rwell ) = ( 1.89e-11 ) ; ( R ) = ( 4.42e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0451418 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588554 +Time: 5.06637e+07s, dt:201453s, Cycle: 427 +well_1Control: BHP (at the specified reference elevation): 24322036.279558495 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 1.58e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.86e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 6.71e-08 ) ; ( R ) = ( 7.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 6.69e-08 ) ; ( R ) = ( 9.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.47e-02 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 8.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 6.77e-08 ) ; ( R ) = ( 8.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 4.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.37e-02 ) ; ( Rwell ) = ( 6.75e-08 ) ; ( R ) = ( 8.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 6.75e-08 ) ; ( R ) = ( 6.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 6.75e-08 ) ; ( R ) = ( 7.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 6.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 6.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 9.93e-10 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 9.18e-10 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 7.92e-12 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0450139 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0580256 +Time: 5.08651e+07s, dt:134870s, Cycle: 428 +well_1Control: BHP (at the specified reference elevation): 24334699.039473876 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 2.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.64e-09 ) ; ( R ) = ( 4.17e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 6.76e-10 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.28e-03 ) ; ( Rwell ) = ( 2.86e-10 ) ; ( R ) = ( 5.28e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.76e-05 ) ; ( Rwell ) = ( 4.24e-13 ) ; ( R ) = ( 5.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311852 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.040358 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.1e+07s, dt:187921s, Cycle: 429 +well_1Control: BHP (at the specified reference elevation): 24343413.0201455 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 6.02e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 4.94e-09 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.75e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 4.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 4.05e-09 ) ; ( R ) = ( 1.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 4.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.41e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 9.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.49e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.55e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; ( R ) = ( 8.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 7.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 6.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 1.79e-09 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 5.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 9.78e-10 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.49e-04 ) ; ( Rwell ) = ( 1.36e-11 ) ; ( R ) = ( 3.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0418864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0556714 +well_1Control: BHP (at the specified reference elevation): 24355296.49969597 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.44853e+07, 1.45246e+07, 1.45637e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 1.97934e+06, 2.05765e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.206 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.93581, 727.27 } rm^3 +compflowStatistics, reservoir: Phase mass: { 981.397, 703079 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 243.05, 211783 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 738.346, 491296 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 18.5856, 0.0675553 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 962.811, 703079 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 981.397, 0 }, { 532.082, 702536 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.44357e+07, 1.44698e+07, 1.4504e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.92967e+06, 1.998e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.091 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.091 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215625 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64687.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150937 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215625 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.000169122, 215625 } } kg +compflowStatistics: Max phase CFL number: 2.91726 +compflowStatistics: Max component CFL number: 97.3803 +Time: 5.11879e+07s, dt:187921s, Cycle: 430 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.79e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 8.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 6.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.67e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 8.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 7.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 6.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 8.51e-10 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 7.25e-10 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.47e-04 ) ; ( Rwell ) = ( 2.15e-11 ) ; ( R ) = ( 3.47e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0423979 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0551689 +Time: 5.13758e+07s, dt:187921s, Cycle: 431 +well_1Control: BHP (at the specified reference elevation): 24367263.92965398 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 5.93e-08 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 4.92e-09 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 7.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 2.57e-09 ) ; ( R ) = ( 7.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.68e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 7.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.66e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.41e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 7.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 7.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 1.57e-09 ) ; ( R ) = ( 6.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 6.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 6.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 9.98e-10 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 8.64e-10 ) ; ( R ) = ( 5.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 7.71e-10 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 6.84e-10 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 5.93e-10 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 3.05e-04 ) ; ( Rwell ) = ( 9.14e-12 ) ; ( R ) = ( 3.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0420305 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544377 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.15638e+07s, dt:93960.3s, Cycle: 432 +well_1Control: BHP (at the specified reference elevation): 24379147.684055515 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 8.99e-10 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.39e-03 ) ; ( Rwell ) = ( 4.77e-10 ) ; ( R ) = ( 8.39e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-04 ) ; ( Rwell ) = ( 4.17e-12 ) ; ( R ) = ( 2.26e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.022281 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0280384 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.16577e+07s, dt:156505s, Cycle: 433 +well_1Control: BHP (at the specified reference elevation): 24385269.595063202 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 6.06e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.60e-09 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 9.18e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 1.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0350195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0496338 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.18142e+07s, dt:185773s, Cycle: 434 +well_1Control: BHP (at the specified reference elevation): 24395210.81249159 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 4.77e-09 ) ; ( R ) = ( 1.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.70e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 8.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.25e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 8.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.37e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 7.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 3.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 6.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 6.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 6.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.36e-09 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 9.69e-10 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 8.66e-10 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 7.18e-10 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 6.47e-10 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 6.04e-10 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 8.87e-05 ) ; ( Rwell ) = ( 7.22e-12 ) ; ( R ) = ( 8.87e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0415806 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0553014 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.2e+07s, dt:92886.4s, Cycle: 435 +well_1Control: BHP (at the specified reference elevation): 24406950.504214466 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 1.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 8.45e-10 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.82e-04 ) ; ( Rwell ) = ( 6.30e-11 ) ; ( R ) = ( 5.82e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0218055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.028068 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.45145e+07, 1.45537e+07, 1.45928e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.01145e+06, 2.08975e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.227 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 2.97596, 727.251 } rm^3 +compflowStatistics, reservoir: Phase mass: { 997.693, 703078 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 248.122, 211794 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 749.571, 491284 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 19.2881, 0.0675579 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 978.405, 703078 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 997.693, 0 }, { 542.542, 702525 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.44648e+07, 1.44989e+07, 1.45332e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.96183e+06, 2.03011e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.097 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.097 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215636 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64690.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150945 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215636 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.00154987, 215636 } } kg +well_1Control: BHP (at the specified reference elevation): 24412988.972639564 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.44907 +compflowStatistics: Max component CFL number: 47.9961 +Time: 5.20929e+07s, dt:154644s, Cycle: 436 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 3.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 3.50e-09 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 9.09e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 9.10e-12 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0345382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0465244 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.22475e+07s, dt:199175s, Cycle: 437 +well_1Control: BHP (at the specified reference elevation): 24422842.976212718 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 8.33e-08 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.42e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 8.26e-08 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.71e-02 ) ; ( Rwell ) = ( 8.32e-08 ) ; ( R ) = ( 9.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.76e-02 ) ; ( Rwell ) = ( 8.28e-08 ) ; ( R ) = ( 8.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 8.27e-08 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 7.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.05e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 7.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.44e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 6.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.76e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 6.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 5.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 9.96e-10 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 7.92e-12 ) ; ( R ) = ( 5.10e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24435343.84295334 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0442623 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612753 +Time: 5.24467e+07s, dt:199175s, Cycle: 438 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 4.69e-09 ) ; ( R ) = ( 1.70e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 4.38e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 4.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.97e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 8.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.96e-02 ) ; ( Rwell ) = ( 2.82e-09 ) ; ( R ) = ( 8.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.33e-02 ) ; ( Rwell ) = ( 2.48e-09 ) ; ( R ) = ( 8.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.18e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 8.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.98e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 8.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.56e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 8.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 1.27e-09 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 1.37e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 9.53e-10 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 1.77e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 8.53e-10 ) ; ( R ) = ( 5.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 7.94e-10 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 2.94e-04 ) ; ( Rwell ) = ( 8.38e-12 ) ; ( R ) = ( 2.94e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0443292 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727349 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.26459e+07s, dt:99587.3s, Cycle: 439 +well_1Control: BHP (at the specified reference elevation): 24447814.2756954 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 2.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 8.98e-10 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.98e-04 ) ; ( Rwell ) = ( 7.84e-11 ) ; ( R ) = ( 4.98e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0231545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.035102 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.27455e+07s, dt:149164s, Cycle: 440 +well_1Control: BHP (at the specified reference elevation): 24454221.2224132 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 5.97e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 3.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 8.07e-10 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.25e-04 ) ; ( Rwell ) = ( 1.18e-11 ) ; ( R ) = ( 4.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.06e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24463775.004330587 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0336173 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0509644 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.28946e+07s, dt:105370s, Cycle: 441 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 7.86e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 1.35e-10 ) ; ( R ) = ( 4.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.20e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24470574.246166922 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0241693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.034965 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.3e+07s, dt:158134s, Cycle: 442 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.58e-09 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 7.08e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.49e-04 ) ; ( Rwell ) = ( 3.08e-11 ) ; ( R ) = ( 5.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0350799 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0510771 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.45486e+07, 1.45879e+07, 1.46269e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.0436e+06, 2.12189e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.252 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.02292, 727.229 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1016.85, 703078 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 254.002, 211808 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 762.851, 491270 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 20.0987, 0.0675608 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 996.754, 703078 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1016.85, 0 }, { 554.871, 702512 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.4499e+07, 1.4533e+07, 1.45673e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 1.99395e+06, 2.06226e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.105 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.105 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215649 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64694.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150954 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215649 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.00897808, 215649 } } kg +well_1Control: BHP (at the specified reference elevation): 24480545.064902417 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.4549 +compflowStatistics: Max component CFL number: 81.4383 +Time: 5.31581e+07s, dt:192897s, Cycle: 443 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 4.91e-09 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.44e-02 ) ; ( Rwell ) = ( 2.69e-09 ) ; ( R ) = ( 9.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.51e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.02e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 8.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.39e-02 ) ; ( Rwell ) = ( 2.30e-09 ) ; ( R ) = ( 8.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.78e-02 ) ; ( Rwell ) = ( 1.95e-09 ) ; ( R ) = ( 8.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.71e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 7.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 7.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.40e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 7.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.62e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 7.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 7.27e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 7.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 9.60e-10 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 8.89e-10 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 8.97e-10 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.67e-04 ) ; ( Rwell ) = ( 3.77e-12 ) ; ( R ) = ( 3.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0432707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644334 +Time: 5.3351e+07s, dt:192897s, Cycle: 444 +well_1Control: BHP (at the specified reference elevation): 24492709.841201164 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 4.74e-09 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.67e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 4.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.92e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 8.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.72e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 7.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 7.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 6.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 6.90e-12 ) ; ( R ) = ( 4.29e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0427785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695091 +Time: 5.35439e+07s, dt:192897s, Cycle: 445 +well_1Control: BHP (at the specified reference elevation): 24504818.474792786 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 4.63e-09 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 4.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 8.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 2.23e-09 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 7.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 1.81e-09 ) ; ( R ) = ( 5.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 8.06e-10 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 1.17e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 7.21e-10 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 6.50e-10 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.27e-04 ) ; ( Rwell ) = ( 1.56e-11 ) ; ( R ) = ( 1.27e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0425296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0698954 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.37368e+07s, dt:96448.7s, Cycle: 446 +well_1Control: BHP (at the specified reference elevation): 24516871.926401265 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 2.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.73e-03 ) ; ( Rwell ) = ( 4.64e-10 ) ; ( R ) = ( 6.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.48e-04 ) ; ( Rwell ) = ( 1.96e-12 ) ; ( R ) = ( 1.48e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.65e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24523084.250040375 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0223092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0336802 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.38333e+07s, dt:147453s, Cycle: 447 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 3.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 6.06e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 7.24e-10 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.06e-04 ) ; ( Rwell ) = ( 1.44e-11 ) ; ( R ) = ( 3.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.46e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24532531.069791555 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0332601 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0486047 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.39807e+07s, dt:19271.7s, Cycle: 448 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 4.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.92e-03 ) ; ( Rwell ) = ( 4.89e-11 ) ; ( R ) = ( 3.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.53e-05 ) ; ( Rwell ) = ( 5.80e-13 ) ; ( R ) = ( 5.53e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00534217 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00664171 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 5.4e+07s, dt:38543.4s, Cycle: 449 +well_1Control: BHP (at the specified reference elevation): 24533803.691077523 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 6.10e-08 ) ; ( R ) = ( 9.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 6.77e-11 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-05 ) ; ( Rwell ) = ( 3.34e-12 ) ; ( R ) = ( 1.37e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00931981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0136739 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.45768e+07, 1.46161e+07, 1.46551e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.07554e+06, 2.15383e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.273 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.06175, 727.211 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1032.78, 703078 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 258.894, 211819 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 773.883, 491258 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 21.0003, 0.0675633 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1011.78, 703078 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1032.78, 0 }, { 564.962, 702501 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.45272e+07, 1.45612e+07, 1.45955e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.02599e+06, 2.0942e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.111 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.111 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215660 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64697.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150962 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215660 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.024681, 215660 } } kg +well_1Control: BHP (at the specified reference elevation): 24536348.664649688 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.600855 +compflowStatistics: Max component CFL number: 19.7952 +Time: 5.40385e+07s, dt:77086.8s, Cycle: 450 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 6.10e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 7.36e-10 ) ; ( R ) = ( 1.32e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-04 ) ; ( Rwell ) = ( 9.19e-12 ) ; ( R ) = ( 3.13e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0174006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0284306 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.41156e+07s, dt:127606s, Cycle: 451 +well_1Control: BHP (at the specified reference elevation): 24541329.866333753 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 5.97e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 2.41e-09 ) ; ( R ) = ( 4.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.70e-10 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.96e-04 ) ; ( Rwell ) = ( 4.10e-12 ) ; ( R ) = ( 2.96e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284194 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.050957 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.42432e+07s, dt:155876s, Cycle: 452 +well_1Control: BHP (at the specified reference elevation): 24549413.918093897 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 8.03e-10 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 3.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0344524 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0590449 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.43991e+07s, dt:174033s, Cycle: 453 +well_1Control: BHP (at the specified reference elevation): 24559206.05930521 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 4.03e-09 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 6.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 6.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 8.47e-10 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 7.21e-10 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 6.70e-10 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 6.54e-10 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.47e-10 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.69e-05 ) ; ( Rwell ) = ( 9.01e-12 ) ; ( R ) = ( 3.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0384278 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626719 +Time: 5.45731e+07s, dt:174033s, Cycle: 454 +well_1Control: BHP (at the specified reference elevation): 24570127.93637122 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 4.08e-09 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 6.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 5.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 9.55e-10 ) ; ( R ) = ( 5.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 8.71e-10 ) ; ( R ) = ( 4.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 7.79e-10 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 1.00e-11 ) ; ( R ) = ( 4.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0386203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604964 +Time: 5.47472e+07s, dt:174033s, Cycle: 455 +well_1Control: BHP (at the specified reference elevation): 24581047.662887696 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.79e-02 ) ; ( Rwell ) = ( 3.73e-09 ) ; ( R ) = ( 9.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 6.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 5.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 8.54e-10 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 7.51e-10 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 7.24e-10 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.09e-04 ) ; ( Rwell ) = ( 7.26e-12 ) ; ( R ) = ( 3.09e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0386446 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660952 +Time: 5.49212e+07s, dt:78788.4s, Cycle: 456 +well_1Control: BHP (at the specified reference elevation): 24591993.035927165 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 2.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 6.35e-10 ) ; ( R ) = ( 1.41e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 2.93e-11 ) ; ( R ) = ( 5.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.018159 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0292212 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.5e+07s, dt:128817s, Cycle: 457 +well_1Control: BHP (at the specified reference elevation): 24597051.636965342 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 4.73e-12 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0467985 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.46116e+07, 1.46508e+07, 1.46899e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.10749e+06, 2.18577e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.298 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.10965, 727.188 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1052.52, 703077 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 264.757, 211833 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 787.765, 491244 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 21.8567, 0.0675663 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1030.66, 703077 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1052.52, 0 }, { 577.416, 702488 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.45621e+07, 1.45961e+07, 1.46303e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.05803e+06, 2.12615e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.119 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.119 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215673 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64701.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150971 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215673 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.062196, 215673 } } kg +well_1Control: BHP (at the specified reference elevation): 24605193.80109335 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.98894 +compflowStatistics: Max component CFL number: 65.9346 +Time: 5.51288e+07s, dt:165355s, Cycle: 458 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.49e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 9.66e-10 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-04 ) ; ( Rwell ) = ( 1.19e-11 ) ; ( R ) = ( 3.35e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0362647 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0611316 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.52942e+07s, dt:180609s, Cycle: 459 +well_1Control: BHP (at the specified reference elevation): 24615528.13567868 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.56e-08 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.91e-04 ) ; ( Rwell ) = ( 1.20e-11 ) ; ( R ) = ( 9.91e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0401845 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654227 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.54748e+07s, dt:188842s, Cycle: 460 +well_1Control: BHP (at the specified reference elevation): 24626877.392743066 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 4.60e-09 ) ; ( R ) = ( 1.10e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.54e-09 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 1.99e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 6.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; ( R ) = ( 6.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 6.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 9.35e-10 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 8.36e-10 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 7.61e-10 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 6.85e-10 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 6.21e-10 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 5.94e-10 ) ; ( R ) = ( 4.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 7.85e-12 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0418514 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0704769 +coupledFlowAndWells: Newton solver converged in more than 14 iterations, time-step required will be decreased. +Time: 5.56636e+07s, dt:94420.8s, Cycle: 461 +well_1Control: BHP (at the specified reference elevation): 24638762.583879627 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 2.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 7.56e-10 ) ; ( R ) = ( 1.96e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.95e-04 ) ; ( Rwell ) = ( 6.87e-11 ) ; ( R ) = ( 5.95e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0217109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0354662 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.5758e+07s, dt:140694s, Cycle: 462 +well_1Control: BHP (at the specified reference elevation): 24644835.63934189 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 3.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 4.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 5.91e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-04 ) ; ( Rwell ) = ( 9.91e-12 ) ; ( R ) = ( 1.78e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311625 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0517779 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.58987e+07s, dt:101262s, Cycle: 463 +well_1Control: BHP (at the specified reference elevation): 24653770.90574549 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 2.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.40e-04 ) ; ( Rwell ) = ( 2.64e-11 ) ; ( R ) = ( 4.40e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0227082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0368 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.6e+07s, dt:148085s, Cycle: 464 +well_1Control: BHP (at the specified reference elevation): 24660222.971058026 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 7.73e-10 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-04 ) ; ( Rwell ) = ( 7.26e-12 ) ; ( R ) = ( 3.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.03298 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0558383 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.46441e+07, 1.46834e+07, 1.47224e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.13939e+06, 2.21766e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.322 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.15454, 727.167 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1071.12, 703077 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 270.395, 211846 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 800.724, 491230 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 22.8047, 0.0675692 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1048.31, 703076 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1071.12, 0 }, { 588.897, 702476 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.45947e+07, 1.46286e+07, 1.46628e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.08994e+06, 2.15805e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.126 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.126 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215685 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64705.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150980 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215685 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.120819, 215685 } } kg +well_1Control: BHP (at the specified reference elevation): 24669592.269348264 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.28889 +compflowStatistics: Max component CFL number: 75.5578 +Time: 5.61481e+07s, dt:171171s, Cycle: 465 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.59e-02 ) ; ( Rwell ) = ( 3.95e-09 ) ; ( R ) = ( 8.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 8.83e-10 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 8.23e-10 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.62e-04 ) ; ( Rwell ) = ( 1.66e-11 ) ; ( R ) = ( 3.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0379608 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632099 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.63193e+07s, dt:183006s, Cycle: 466 +well_1Control: BHP (at the specified reference elevation): 24680402.676447853 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 4.15e-09 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; ( R ) = ( 6.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 5.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 9.41e-10 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 8.41e-10 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 7.51e-10 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 6.41e-10 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 5.83e-10 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 7.16e-05 ) ; ( Rwell ) = ( 1.23e-11 ) ; ( R ) = ( 7.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24691934.88134496 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0404064 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065783 +Time: 5.65023e+07s, dt:183006s, Cycle: 467 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 4.22e-09 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.71e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 7.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 6.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 5.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 9.35e-10 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 7.98e-10 ) ; ( R ) = ( 5.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 7.47e-10 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 6.61e-10 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 3.69e-04 ) ; ( Rwell ) = ( 1.04e-11 ) ; ( R ) = ( 3.69e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0401311 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656319 +Time: 5.66853e+07s, dt:183006s, Cycle: 468 +well_1Control: BHP (at the specified reference elevation): 24703415.141305335 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 4.09e-09 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 2.38e-09 ) ; ( R ) = ( 6.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 6.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.99e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 7.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 6.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 1.29e-09 ) ; ( R ) = ( 6.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 9.92e-10 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 8.96e-10 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 8.00e-10 ) ; ( R ) = ( 5.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 8.32e-10 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.39e-04 ) ; ( Rwell ) = ( 5.32e-12 ) ; ( R ) = ( 1.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0404936 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662149 +Time: 5.68683e+07s, dt:131727s, Cycle: 469 +well_1Control: BHP (at the specified reference elevation): 24714930.046564978 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 3.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 2.02e-09 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.17e-04 ) ; ( Rwell ) = ( 3.55e-11 ) ; ( R ) = ( 9.17e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0296124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0474863 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.7e+07s, dt:167681s, Cycle: 470 +well_1Control: BHP (at the specified reference elevation): 24723333.95918986 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 8.62e-08 ) ; ( R ) = ( 4.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 6.72e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 9.02e-10 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.92e-04 ) ; ( Rwell ) = ( 1.61e-11 ) ; ( R ) = ( 4.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0369817 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0622371 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.46766e+07, 1.47158e+07, 1.47549e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.17126e+06, 2.24952e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.345 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.19947, 727.146 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1089.83, 703076 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 275.996, 211859 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 813.831, 491217 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 23.7488, 0.0675721 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1066.08, 703076 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1089.83, 0 }, { 600.249, 702464 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.46272e+07, 1.46611e+07, 1.46953e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.12186e+06, 2.18991e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.133 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.133 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215698 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64709.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150988 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215698 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.208045, 215697 } } kg +well_1Control: BHP (at the specified reference elevation): 24733939.229713883 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.58672 +compflowStatistics: Max component CFL number: 85.2879 +Time: 5.71677e+07s, dt:181067s, Cycle: 471 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 4.04e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.52e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 7.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 1.60e-09 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 9.59e-10 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 8.83e-10 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 7.58e-10 ) ; ( R ) = ( 5.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 7.65e-10 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 6.46e-10 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.39e-04 ) ; ( Rwell ) = ( 1.14e-11 ) ; ( R ) = ( 2.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0399954 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670642 +Time: 5.73487e+07s, dt:181067s, Cycle: 472 +well_1Control: BHP (at the specified reference elevation): 24745383.76171024 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 3.62e-09 ) ; ( R ) = ( 1.28e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.28e-09 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 6.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 1.40e-09 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 3.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 9.72e-10 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 8.71e-10 ) ; ( R ) = ( 3.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 7.96e-10 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 1.96e-11 ) ; ( R ) = ( 6.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0401764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662811 +Time: 5.75298e+07s, dt:181067s, Cycle: 473 +well_1Control: BHP (at the specified reference elevation): 24756855.971077926 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 6.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.35e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 6.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 3.36e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 5.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 3.15e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 8.73e-10 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 7.83e-10 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 7.12e-10 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 6.42e-10 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 6.87e-10 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.91e-04 ) ; ( Rwell ) = ( 3.00e-12 ) ; ( R ) = ( 1.91e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0403673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644894 +Time: 5.77109e+07s, dt:181067s, Cycle: 474 +well_1Control: BHP (at the specified reference elevation): 24768391.670603644 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.12e-09 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 9.67e-10 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 8.68e-10 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 7.82e-10 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 7.02e-10 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 6.42e-10 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 5.66e-10 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.16e-10 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 9.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 4.72e-10 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.22e-04 ) ; ( Rwell ) = ( 6.81e-12 ) ; ( R ) = ( 2.22e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0401988 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066405 +Time: 5.7892e+07s, dt:108050s, Cycle: 475 +well_1Control: BHP (at the specified reference elevation): 24779853.632511083 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.98e-04 ) ; ( Rwell ) = ( 3.29e-11 ) ; ( R ) = ( 8.98e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0242531 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0420255 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.8e+07s, dt:147291s, Cycle: 476 +well_1Control: BHP (at the specified reference elevation): 24786747.187825136 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 3.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 4.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 6.25e-10 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-04 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 2.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0322266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0549053 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.47079e+07, 1.47472e+07, 1.47862e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.20327e+06, 2.28153e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.368 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.24303, 727.125 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1108.04, 703075 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 281.203, 211872 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 826.835, 491203 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 24.4223, 0.0675749 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1083.62, 703075 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1108.04, 0 }, { 610.885, 702452 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.46585e+07, 1.46924e+07, 1.47266e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.15378e+06, 2.22193e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.14 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.14 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215709 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64712.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150997 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215709 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.324105, 215709 } } kg +well_1Control: BHP (at the specified reference elevation): 24796016.556756087 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.27405 +compflowStatistics: Max component CFL number: 74.6912 +Time: 5.81473e+07s, dt:172021s, Cycle: 477 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; ( R ) = ( 4.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.79e-02 ) ; ( Rwell ) = ( 3.72e-09 ) ; ( R ) = ( 7.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 9.35e-10 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.00e-04 ) ; ( Rwell ) = ( 1.80e-11 ) ; ( R ) = ( 2.00e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0381436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663431 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.83193e+07s, dt:178228s, Cycle: 478 +well_1Control: BHP (at the specified reference elevation): 24806865.88580575 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 4.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 1.98e-09 ) ; ( R ) = ( 6.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 3.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 5.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 3.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 2.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 1.00e-09 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 8.57e-10 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 7.74e-10 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 6.90e-10 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.09e-04 ) ; ( Rwell ) = ( 1.43e-11 ) ; ( R ) = ( 2.09e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0395491 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0705539 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.84975e+07s, dt:177293s, Cycle: 479 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.95e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; ( R ) = ( 9.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; +well_1Control: BHP (at the specified reference elevation): 24818176.047810536 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; ( R ) = ( 5.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 3.24e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 3.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 4.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 4.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 9.11e-10 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 8.21e-10 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.71e-05 ) ; ( Rwell ) = ( 1.83e-11 ) ; ( R ) = ( 7.71e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0394854 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0670243 +Time: 5.86748e+07s, dt:177293s, Cycle: 480 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.78e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 24829481.391939804 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.09e-02 ) ; ( Rwell ) = ( 3.80e-09 ) ; ( R ) = ( 7.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 8.98e-10 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.98e-04 ) ; ( Rwell ) = ( 3.68e-11 ) ; ( R ) = ( 1.98e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0394087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676456 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.88521e+07s, dt:147873s, Cycle: 481 +well_1Control: BHP (at the specified reference elevation): 24840755.14498192 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 7.96e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.68e-04 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 4.68e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0332789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557133 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.9e+07s, dt:171162s, Cycle: 482 +well_1Control: BHP (at the specified reference elevation): 24850226.193029888 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.06e-02 ) ; ( Rwell ) = ( 1.89e-09 ) ; ( R ) = ( 6.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 5.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 1.72e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 8.68e-10 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 8.60e-10 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 7.44e-12 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0378007 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715587 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.47408e+07, 1.478e+07, 1.4819e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.23531e+06, 2.31357e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.392 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.28887, 727.103 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1127.29, 703074 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 286.71, 211885 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 840.582, 491189 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 25.5062, 0.0675779 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1101.79, 703074 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1127.29, 0 }, { 621.742, 702440 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.46912e+07, 1.47253e+07, 1.47594e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.18576e+06, 2.25397e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.147 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.147 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215722 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64716.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151005 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215722 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.486414, 215721 } } kg +well_1Control: BHP (at the specified reference elevation): 24861084.940903045 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.65246 +compflowStatistics: Max component CFL number: 86.5218 +Time: 5.91712e+07s, dt:168658s, Cycle: 483 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 5.77e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 3.56e-09 ) ; ( R ) = ( 5.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 8.82e-10 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-04 ) ; ( Rwell ) = ( 2.10e-11 ) ; ( R ) = ( 2.98e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0376861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658656 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.93398e+07s, dt:175571s, Cycle: 484 +well_1Control: BHP (at the specified reference elevation): 24871864.091349833 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.23e-02 ) ; ( Rwell ) = ( 3.48e-09 ) ; ( R ) = ( 9.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.28e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 9.59e-10 ) ; ( R ) = ( 5.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.20e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 8.54e-10 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 1.85e-11 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0392145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681518 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.95154e+07s, dt:178717s, Cycle: 485 +well_1Control: BHP (at the specified reference elevation): 24883126.12732903 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 3.64e-09 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.70e-02 ) ; ( Rwell ) = ( 2.25e-09 ) ; ( R ) = ( 7.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 6.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 9.33e-10 ) ; ( R ) = ( 4.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 7.85e-10 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 6.94e-10 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 1.16e-11 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0400975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0709445 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.96941e+07s, dt:177124s, Cycle: 486 +well_1Control: BHP (at the specified reference elevation): 24894615.192365665 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-04 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 1.77e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0393224 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737041 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.98712e+07s, dt:128768s, Cycle: 487 +well_1Control: BHP (at the specified reference elevation): 24905884.789187275 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 3.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 6.31e-10 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 8.22e-12 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 24914091.86649058 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0286666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0502416 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6e+07s, dt:158616s, Cycle: 488 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 4.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 2.89e-12 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0346647 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651999 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.47726e+07, 1.48118e+07, 1.48508e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.26754e+06, 2.3458e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.415 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.3335, 727.081 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1146.11, 703072 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 291.755, 211897 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 854.359, 491175 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 26.309, 0.0675807 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1119.8, 703072 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1146.11, 0 }, { 631.91, 702428 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.4723e+07, 1.47571e+07, 1.47912e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.21787e+06, 2.2862e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.154 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.154 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215734 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64720.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151014 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215734 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.692902, 215733 } } kg +well_1Control: BHP (at the specified reference elevation): 24924080.52444922 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.45756 +compflowStatistics: Max component CFL number: 79.9358 +Time: 6.01586e+07s, dt:166214s, Cycle: 489 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; ( R ) = ( 5.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 5.99e-12 ) ; ( R ) = ( 2.83e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0372944 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688882 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.03248e+07s, dt:167993s, Cycle: 490 +well_1Control: BHP (at the specified reference elevation): 24934700.455144644 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; ( R ) = ( 4.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.90e-04 ) ; ( Rwell ) = ( 5.91e-11 ) ; ( R ) = ( 3.90e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0377249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0733527 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.04928e+07s, dt:162795s, Cycle: 491 +well_1Control: BHP (at the specified reference elevation): 24945491.247536898 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; ( R ) = ( 4.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 2.23e-11 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.32e-06 ) ; ( Rwell ) = ( 1.73e-14 ) ; ( R ) = ( 7.32e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0365474 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664429 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.06556e+07s, dt:168503s, Cycle: 492 +well_1Control: BHP (at the specified reference elevation): 24956006.192224875 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 3.52e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 9.76e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.21e-04 ) ; ( Rwell ) = ( 9.06e-12 ) ; ( R ) = ( 7.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.037613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0693579 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.08241e+07s, dt:169540s, Cycle: 493 +well_1Control: BHP (at the specified reference elevation): 24966841.537645467 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 9.68e-10 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-04 ) ; ( Rwell ) = ( 1.68e-11 ) ; ( R ) = ( 2.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0380105 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715058 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.09937e+07s, dt:6338.65s, Cycle: 494 +well_1Control: BHP (at the specified reference elevation): 24977733.70734615 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 1.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 2.97e-11 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-06 ) ; ( Rwell ) = ( 1.41e-13 ) ; ( R ) = ( 1.71e-06 ) ; + Last LinSolve(iter,res) = ( 8, 4.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00225363 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00264471 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.1e+07s, dt:12677.3s, Cycle: 495 +well_1Control: BHP (at the specified reference elevation): 24978148.84948548 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.69e-03 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 3.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 2.27e-12 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00328181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00525537 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.48003e+07, 1.48395e+07, 1.48785e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.29987e+06, 2.37812e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.435 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.37267, 727.062 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1162.69, 703071 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 296.194, 211908 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 866.499, 491162 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 27.0457, 0.0675831 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1135.65, 703070 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1162.69, 0 }, { 640.355, 702417 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.47505e+07, 1.47847e+07, 1.4819e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.25007e+06, 2.31853e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.16 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.16 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215745 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64723.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151021 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215745 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 0.920384, 215744 } } kg +well_1Control: BHP (at the specified reference elevation): 24978992.59968073 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.198544 +compflowStatistics: Max component CFL number: 6.37191 +Time: 6.10127e+07s, dt:25354.6s, Cycle: 496 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.35e-03 ) ; ( Rwell ) = ( 6.02e-08 ) ; ( R ) = ( 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 7.62e-11 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.61e-05 ) ; ( Rwell ) = ( 2.04e-12 ) ; ( R ) = ( 5.61e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0062392 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0106164 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.1038e+07s, dt:50709.2s, Cycle: 497 +well_1Control: BHP (at the specified reference elevation): 24980686.69361765 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 6.04e-08 ) ; ( R ) = ( 1.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.74e-03 ) ; ( Rwell ) = ( 3.16e-10 ) ; ( R ) = ( 9.74e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 3.37e-12 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0118549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0214611 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.10887e+07s, dt:94303.2s, Cycle: 498 +well_1Control: BHP (at the specified reference elevation): 24984057.36083853 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 6.01e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-04 ) ; ( Rwell ) = ( 8.77e-12 ) ; ( R ) = ( 2.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0213283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0412559 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.1183e+07s, dt:129850s, Cycle: 499 +well_1Control: BHP (at the specified reference elevation): 24990221.10030747 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; ( R ) = ( 3.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.20e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-03 ) ; ( Rwell ) = ( 5.08e-12 ) ; ( R ) = ( 1.46e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.25e-07 ) ; ( Rwell ) = ( 2.86e-15 ) ; ( R ) = ( 9.25e-07 ) ; + Last LinSolve(iter,res) = ( 8, 1.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0288218 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0560856 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.13129e+07s, dt:149686s, Cycle: 500 +well_1Control: BHP (at the specified reference elevation): 24998547.810420815 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 7.70e-10 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-04 ) ; ( Rwell ) = ( 5.01e-12 ) ; ( R ) = ( 3.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25008055.87643479 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0329567 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641368 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.14626e+07s, dt:158539s, Cycle: 501 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 8.62e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.13e-03 ) ; ( Rwell ) = ( 3.22e-10 ) ; ( R ) = ( 7.13e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.67e-05 ) ; ( Rwell ) = ( 6.86e-13 ) ; ( R ) = ( 7.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0355209 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692221 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.16211e+07s, dt:159722s, Cycle: 502 +well_1Control: BHP (at the specified reference elevation): 25018176.12809281 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 5.33e-08 ) ; ( R ) = ( 6.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 4.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 8.54e-10 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.07e-04 ) ; ( Rwell ) = ( 1.17e-11 ) ; ( R ) = ( 4.07e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0357554 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688831 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.17808e+07s, dt:161440s, Cycle: 503 +well_1Control: BHP (at the specified reference elevation): 25028423.360220946 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 2.89e-09 ) ; ( R ) = ( 5.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 9.24e-10 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.31e-04 ) ; ( Rwell ) = ( 9.87e-12 ) ; ( R ) = ( 5.31e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0358373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684739 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.19423e+07s, dt:57718s, Cycle: 504 +well_1Control: BHP (at the specified reference elevation): 25038761.838887572 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 1.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.76e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 3.32e-11 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.65e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25042534.666398447 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0135376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0255097 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.2e+07s, dt:100156s, Cycle: 505 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 5.90e-08 ) ; ( R ) = ( 3.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 6.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25049038.567279287 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0225968 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0419505 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.48356e+07, 1.48749e+07, 1.49139e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.33235e+06, 2.4106e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.461 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.42284, 727.038 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1184.02, 703068 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 301.524, 211922 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 882.492, 491146 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 28.1891, 0.0675863 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1155.83, 703068 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1184.02, 0 }, { 650.822, 702404 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.47857e+07, 1.482e+07, 1.48543e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.28246e+06, 2.35102e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.168 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.168 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215758 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64727.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151031 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215758 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 1.28418, 215757 } } kg +compflowStatistics: Max phase CFL number: 1.57177 +compflowStatistics: Max component CFL number: 50.1711 +Time: 6.21002e+07s, dt:136664s, Cycle: 506 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 2.31e-09 ) ; ( R ) = ( 4.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 6.07e-10 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.38e-05 ) ; ( Rwell ) = ( 8.87e-12 ) ; ( R ) = ( 6.38e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.060911 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.22368e+07s, dt:149615s, Cycle: 507 +well_1Control: BHP (at the specified reference elevation): 25057927.294307705 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 5.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.06e-10 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.96e-04 ) ; ( Rwell ) = ( 9.21e-12 ) ; ( R ) = ( 1.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0340454 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658235 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.23864e+07s, dt:155812s, Cycle: 508 +well_1Control: BHP (at the specified reference elevation): 25067694.15512622 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 8.11e-10 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.20e-05 ) ; ( Rwell ) = ( 7.81e-12 ) ; ( R ) = ( 5.20e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0350982 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672397 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.25422e+07s, dt:160019s, Cycle: 509 +well_1Control: BHP (at the specified reference elevation): 25077825.884632424 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 3.18e-09 ) ; ( R ) = ( 4.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 8.15e-10 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 8.70e-12 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0354604 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688532 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.27023e+07s, dt:161786s, Cycle: 510 +well_1Control: BHP (at the specified reference elevation): 25088086.06135318 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 5.77e-08 ) ; ( R ) = ( 4.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 3.33e-09 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 8.47e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-05 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 6.55e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.96e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25098454.616070237 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.036168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.071537 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.28641e+07s, dt:135949s, Cycle: 511 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 4.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.24e-09 ) ; ( R ) = ( 3.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 1.77e-11 ) ; ( R ) = ( 4.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0308358 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059701 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.3e+07s, dt:150734s, Cycle: 512 +well_1Control: BHP (at the specified reference elevation): 25107294.02006863 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 2.66e-11 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.46e-06 ) ; ( Rwell ) = ( 1.28e-14 ) ; ( R ) = ( 4.46e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0337967 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642164 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.487e+07, 1.49092e+07, 1.49482e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.36502e+06, 2.44327e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.486 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.47191, 727.014 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1204.96, 703065 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 306.678, 211936 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 898.279, 491129 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 29.2377, 0.0675893 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1175.72, 703065 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1204.96, 0 }, { 660.503, 702392 } } kg +well_1Control: BHP (at the specified reference elevation): 25117083.137785416 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.48199e+07, 1.48543e+07, 1.48886e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.31498e+06, 2.38369e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.176 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.176 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215771 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64731.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151040 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215771 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 1.72493, 215769 } } kg +compflowStatistics: Max phase CFL number: 2.37499 +compflowStatistics: Max component CFL number: 75.2611 +Time: 6.31507e+07s, dt:159520s, Cycle: 513 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 7.04e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-04 ) ; ( Rwell ) = ( 1.82e-11 ) ; ( R ) = ( 3.59e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.52e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25127420.77425924 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.035954 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069342 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.33103e+07s, dt:160526s, Cycle: 514 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 5.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 9.47e-10 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.61e-05 ) ; ( Rwell ) = ( 7.15e-12 ) ; ( R ) = ( 8.61e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0364484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0713741 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.34708e+07s, dt:158453s, Cycle: 515 +well_1Control: BHP (at the specified reference elevation): 25137889.137792386 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 8.78e-10 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.83e-05 ) ; ( Rwell ) = ( 6.62e-12 ) ; ( R ) = ( 9.83e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0359265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691274 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.36292e+07s, dt:159781s, Cycle: 516 +well_1Control: BHP (at the specified reference elevation): 25148259.983471822 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 8.25e-10 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.95e-04 ) ; ( Rwell ) = ( 9.71e-12 ) ; ( R ) = ( 4.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0362288 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668996 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.3789e+07s, dt:164642s, Cycle: 517 +well_1Control: BHP (at the specified reference elevation): 25158728.21268872 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.49e-03 ) ; ( Rwell ) = ( 3.87e-12 ) ; ( R ) = ( 3.49e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.03e-06 ) ; ( Rwell ) = ( 1.75e-14 ) ; ( R ) = ( 9.03e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0374249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727195 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.39537e+07s, dt:46344.3s, Cycle: 518 +well_1Control: BHP (at the specified reference elevation): 25169513.88953302 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 1.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 3.02e-10 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-05 ) ; ( Rwell ) = ( 5.33e-13 ) ; ( R ) = ( 3.91e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.45e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25172617.515530422 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0113168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0206215 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.4e+07s, dt:87486.9s, Cycle: 519 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 6.00e-08 ) ; ( R ) = ( 2.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 9.66e-10 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-04 ) ; ( Rwell ) = ( 4.35e-12 ) ; ( R ) = ( 2.46e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0201811 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0392743 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.49009e+07, 1.49402e+07, 1.49792e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.39798e+06, 2.47622e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.508 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.51655, 726.992 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1224.08, 703062 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 311.128, 211948 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 912.949, 491114 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 30.0662, 0.0675921 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1194.01, 703062 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1224.08, 0 }, { 668.605, 702380 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.48505e+07, 1.48851e+07, 1.49196e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.34764e+06, 2.41665e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.183 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.183 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215783 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64734.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151048 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215783 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.20008, 215781 } } kg +well_1Control: BHP (at the specified reference elevation): 25178425.919669658 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.39688 +compflowStatistics: Max component CFL number: 43.554 +Time: 6.40875e+07s, dt:123678s, Cycle: 520 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 5.35e-10 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.51e-05 ) ; ( Rwell ) = ( 2.25e-12 ) ; ( R ) = ( 7.51e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0280199 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0537969 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.42112e+07s, dt:146246s, Cycle: 521 +well_1Control: BHP (at the specified reference elevation): 25186553.934868526 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.66e-09 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 6.87e-10 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.10e-04 ) ; ( Rwell ) = ( 6.86e-12 ) ; ( R ) = ( 5.10e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0327953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643327 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.43574e+07s, dt:154590s, Cycle: 522 +well_1Control: BHP (at the specified reference elevation): 25196070.04097824 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.68e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 5.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 8.17e-10 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-04 ) ; ( Rwell ) = ( 4.52e-12 ) ; ( R ) = ( 2.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0351324 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685548 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.4512e+07s, dt:156748s, Cycle: 523 +well_1Control: BHP (at the specified reference elevation): 25206187.095147412 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 9.10e-10 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.60e-04 ) ; ( Rwell ) = ( 5.87e-12 ) ; ( R ) = ( 7.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.71e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25216487.866180174 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0355176 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682412 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.46688e+07s, dt:159418s, Cycle: 524 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 8.99e-10 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 6.39e-12 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.036451 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685836 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.48282e+07s, dt:161598s, Cycle: 525 +well_1Control: BHP (at the specified reference elevation): 25227023.071665168 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 8.38e-10 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-04 ) ; ( Rwell ) = ( 1.34e-11 ) ; ( R ) = ( 2.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0371516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0698992 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.49898e+07s, dt:10233.7s, Cycle: 526 +well_1Control: BHP (at the specified reference elevation): 25237756.23772254 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-03 ) ; ( Rwell ) = ( 5.93e-08 ) ; ( R ) = ( 3.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 6.40e-11 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-06 ) ; ( Rwell ) = ( 4.53e-14 ) ; ( R ) = ( 1.70e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00307946 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00448138 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.5e+07s, dt:20467.5s, Cycle: 527 +well_1Control: BHP (at the specified reference elevation): 25238447.94818101 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.12e-03 ) ; ( Rwell ) = ( 6.04e-08 ) ; ( R ) = ( 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-03 ) ; ( Rwell ) = ( 7.52e-11 ) ; ( R ) = ( 5.20e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 1.71e-12 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00516853 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00898214 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.49319e+07, 1.49711e+07, 1.50101e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.43119e+06, 2.50943e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.531 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.56156, 726.969 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1243.42, 703059 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 315.442, 211960 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 927.981, 491098 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 31.1108, 0.0675948 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1212.31, 703059 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1243.42, 0 }, { 676.285, 702369 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.48813e+07, 1.49161e+07, 1.49506e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.3806e+06, 2.44986e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.19 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.19 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215795 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64738.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151056 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215795 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.75958, 215792 } } kg +well_1Control: BHP (at the specified reference elevation): 25239844.21057038 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 0.32914 +compflowStatistics: Max component CFL number: 10.1596 +Time: 6.50205e+07s, dt:40935s, Cycle: 528 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 6.09e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.54e-03 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 9.54e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.36e-05 ) ; ( Rwell ) = ( 7.27e-12 ) ; ( R ) = ( 7.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00969429 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0181497 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.50614e+07s, dt:80869.1s, Cycle: 529 +well_1Control: BHP (at the specified reference elevation): 25242618.817826465 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 8.62e-10 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 2.07e-10 ) ; ( R ) = ( 9.98e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 2.35e-12 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.06e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25248035.036315557 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0188017 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0360559 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.51423e+07s, dt:119501s, Cycle: 530 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 3.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 1.86e-09 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 3.61e-12 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25255910.571668416 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0269436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0531209 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.52618e+07s, dt:142391s, Cycle: 531 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 6.42e-10 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-04 ) ; ( Rwell ) = ( 9.88e-12 ) ; ( R ) = ( 3.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0323613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631048 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.54042e+07s, dt:152399s, Cycle: 532 +well_1Control: BHP (at the specified reference elevation): 25265300.479206093 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 2.67e-09 ) ; ( R ) = ( 5.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 7.74e-10 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.15e-11 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.25e-06 ) ; ( Rwell ) = ( 1.44e-14 ) ; ( R ) = ( 2.25e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.73e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25275341.35246835 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0347136 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066614 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.55566e+07s, dt:157477s, Cycle: 533 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.04e-09 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-03 ) ; ( Rwell ) = ( 1.30e-11 ) ; ( R ) = ( 1.56e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-06 ) ; ( Rwell ) = ( 5.26e-14 ) ; ( R ) = ( 2.11e-06 ) ; + Last LinSolve(iter,res) = ( 9, 9.72e-04 ) ; +well_1Control: BHP (at the specified reference elevation): 25285694.87531646 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0357628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683089 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.5714e+07s, dt:160055s, Cycle: 534 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.08e-04 ) ; ( Rwell ) = ( 2.92e-11 ) ; ( R ) = ( 8.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0362818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692063 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.58741e+07s, dt:125906s, Cycle: 535 +well_1Control: BHP (at the specified reference elevation): 25296249.88054432 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-04 ) ; ( Rwell ) = ( 2.95e-11 ) ; ( R ) = ( 4.66e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.029024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0539807 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.6e+07s, dt:148573s, Cycle: 536 +well_1Control: BHP (at the specified reference elevation): 25304642.36029652 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 2.47e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 7.63e-10 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.63e-04 ) ; ( Rwell ) = ( 1.09e-11 ) ; ( R ) = ( 5.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.034018 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638942 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.49696e+07, 1.50088e+07, 1.50478e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.46458e+06, 2.54281e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.558 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.61665, 726.941 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1267.2, 703054 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 320.318, 211975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 946.879, 491079 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 32.0707, 0.0675982 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1235.13, 703054 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1267.2, 0 }, { 685.063, 702355 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.49188e+07, 1.49537e+07, 1.49882e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.41383e+06, 2.48325e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.198 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.198 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215809 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64742.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151067 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215809 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 3.56234, 215806 } } kg +well_1Control: BHP (at the specified reference elevation): 25314523.10902383 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 2.39445 +compflowStatistics: Max component CFL number: 73.4869 +Time: 6.61486e+07s, dt:157746s, Cycle: 537 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 8.72e-10 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.58e-05 ) ; ( Rwell ) = ( 1.40e-11 ) ; ( R ) = ( 7.58e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.035854 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681494 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.63063e+07s, dt:160576s, Cycle: 538 +well_1Control: BHP (at the specified reference elevation): 25324960.0695749 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 2.99e-09 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 8.55e-10 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-04 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 3.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0364893 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686063 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.64669e+07s, dt:162736s, Cycle: 539 +well_1Control: BHP (at the specified reference elevation): 25335583.40506701 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 1.78e-07 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 8.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.00e-09 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.91e-03 ) ; ( Rwell ) = ( 8.71e-06 ) ; ( R ) = ( 8.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.54e-05 ) ; ( Rwell ) = ( 2.61e-07 ) ; ( R ) = ( 5.54e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0372634 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668659 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.66296e+07s, dt:167743s, Cycle: 540 +well_1Control: BHP (at the specified reference elevation): 25346415.057630528 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.20e-07 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.61e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.09e-09 ) ; ( R ) = ( 2.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 2.21e-06 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0383519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706391 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.67974e+07s, dt:166728s, Cycle: 541 +well_1Control: BHP (at the specified reference elevation): 25357598.618959382 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 2.27e-06 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.13e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.16e-04 ) ; ( Rwell ) = ( 1.78e-11 ) ; ( R ) = ( 3.16e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0379031 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696251 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.69641e+07s, dt:35898.6s, Cycle: 542 +well_1Control: BHP (at the specified reference elevation): 25368665.923691697 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 1.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.01e-03 ) ; ( Rwell ) = ( 2.00e-10 ) ; ( R ) = ( 7.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.23e-04 ) ; ( Rwell ) = ( 1.25e-12 ) ; ( R ) = ( 5.23e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0088093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0151707 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.7e+07s, dt:71797.1s, Cycle: 543 +well_1Control: BHP (at the specified reference elevation): 25371093.986509837 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 6.00e-08 ) ; ( R ) = ( 2.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 5.45e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-03 ) ; ( Rwell ) = ( 7.95e-12 ) ; ( R ) = ( 1.40e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.67e-05 ) ; ( Rwell ) = ( 2.88e-15 ) ; ( R ) = ( 9.67e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.03e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25375907.273456253 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0166253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0298741 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.50005e+07, 1.50398e+07, 1.50788e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.4981e+06, 2.57633e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.581 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.66218, 726.918 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1286.93, 703050 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 324.136, 211987 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 962.795, 491063 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 33.0976, 0.0676055 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1253.83, 703050 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1286.93, 0 }, { 691.859, 702344 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.49496e+07, 1.49847e+07, 1.50192e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.44719e+06, 2.51677e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.205 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.205 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215821 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64746.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151075 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215821 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 4.32996, 215817 } } kg +compflowStatistics: Max phase CFL number: 1.16277 +compflowStatistics: Max component CFL number: 35.4099 +Time: 6.70718e+07s, dt:116205s, Cycle: 544 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 3.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.66e-09 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.88e-04 ) ; ( Rwell ) = ( 5.30e-12 ) ; ( R ) = ( 3.88e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0264613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0495449 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.7188e+07s, dt:144320s, Cycle: 545 +well_1Control: BHP (at the specified reference elevation): 25383601.618183628 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 2.33e-09 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 6.76e-10 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 1.13e-11 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.27e-06 ) ; ( Rwell ) = ( 6.95e-15 ) ; ( R ) = ( 3.27e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0330434 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0608864 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.73323e+07s, dt:158037s, Cycle: 546 +well_1Control: BHP (at the specified reference elevation): 25393194.42877342 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 8.65e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-04 ) ; ( Rwell ) = ( 9.46e-12 ) ; ( R ) = ( 2.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0364067 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676332 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.74904e+07s, dt:161682s, Cycle: 547 +well_1Control: BHP (at the specified reference elevation): 25403784.751659498 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.22e-09 ) ; ( R ) = ( 5.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 9.06e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 4.91e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.76e-06 ) ; ( Rwell ) = ( 8.08e-16 ) ; ( R ) = ( 3.76e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0371682 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677933 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.7652e+07s, dt:165153s, Cycle: 548 +well_1Control: BHP (at the specified reference elevation): 25414621.32690838 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 9.59e-10 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 2.99e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.29e-05 ) ; ( Rwell ) = ( 1.37e-12 ) ; ( R ) = ( 5.29e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0378107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682588 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.78172e+07s, dt:167937s, Cycle: 549 +well_1Control: BHP (at the specified reference elevation): 25425660.168037713 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 3.20e-09 ) ; ( R ) = ( 5.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 3.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 9.45e-10 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.67e-04 ) ; ( Rwell ) = ( 1.08e-11 ) ; ( R ) = ( 2.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0384206 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0719211 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.79851e+07s, dt:14868.8s, Cycle: 550 +well_1Control: BHP (at the specified reference elevation): 25436901.926305797 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 5.92e-08 ) ; ( R ) = ( 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 9.30e-11 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.92e-06 ) ; ( Rwell ) = ( 9.24e-14 ) ; ( R ) = ( 7.92e-06 ) ; + Last LinSolve(iter,res) = ( 8, 9.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00406178 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00627571 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6.8e+07s, dt:29737.6s, Cycle: 551 +well_1Control: BHP (at the specified reference elevation): 25437916.151861522 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.63e-03 ) ; ( Rwell ) = ( 6.04e-08 ) ; ( R ) = ( 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.00e-03 ) ; ( Rwell ) = ( 1.01e-10 ) ; ( R ) = ( 7.00e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-05 ) ; ( Rwell ) = ( 2.13e-12 ) ; ( R ) = ( 2.50e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00716638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0125174 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +well_1Control: BHP (at the specified reference elevation): 25439947.517330885 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.50328e+07, 1.50721e+07, 1.51111e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.53181e+06, 2.61003e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.604 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.70997, 726.894 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1307.73, 703045 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 328.156, 212000 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 979.569, 491045 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 34.274, 0.0676084 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1273.45, 703045 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1307.73, 0 }, { 698.48, 702333 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.49817e+07, 1.50169e+07, 1.50515e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.48072e+06, 2.55047e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.212 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.212 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215834 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64750.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151084 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215834 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 5.23717, 215828 } } kg +compflowStatistics: Max phase CFL number: 0.484483 +compflowStatistics: Max component CFL number: 14.6221 +Time: 6.80297e+07s, dt:59475.2s, Cycle: 552 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 6.04e-08 ) ; ( R ) = ( 1.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 4.42e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e-05 ) ; ( Rwell ) = ( 1.78e-12 ) ; ( R ) = ( 5.88e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25443995.4855325 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0140463 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0258726 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.80892e+07s, dt:102590s, Cycle: 553 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 6.02e-08 ) ; ( R ) = ( 3.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.72e-04 ) ; ( Rwell ) = ( 5.83e-12 ) ; ( R ) = ( 3.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25450894.75724662 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0235283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0445918 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.81918e+07s, dt:135339s, Cycle: 554 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.13e-09 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 5.93e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.51e-04 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 5.51e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0309929 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0570108 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.83271e+07s, dt:154445s, Cycle: 555 +well_1Control: BHP (at the specified reference elevation): 25459928.762806006 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 5.90e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 7.20e-10 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 7.02e-12 ) ; ( R ) = ( 7.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0353317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0732213 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.84816e+07s, dt:149848s, Cycle: 556 +well_1Control: BHP (at the specified reference elevation): 25470201.373563558 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 2.61e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.86e-04 ) ; ( Rwell ) = ( 1.70e-11 ) ; ( R ) = ( 3.86e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.62e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25480195.464948647 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0343375 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681136 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.86314e+07s, dt:152589s, Cycle: 557 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.34e-03 ) ; ( Rwell ) = ( 1.98e-11 ) ; ( R ) = ( 3.34e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 2.28e-14 ) ; ( R ) = ( 4.70e-04 ) ; + Last LinSolve(iter,res) = ( 7, 2.30e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25490337.00833069 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0345259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664231 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.8784e+07s, dt:157971s, Cycle: 558 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 9.00e-10 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-04 ) ; ( Rwell ) = ( 1.14e-12 ) ; ( R ) = ( 1.15e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.19e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25500835.48019644 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0360052 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728463 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.8942e+07s, dt:58004.2s, Cycle: 559 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 1.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.84e-10 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.46e-05 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 8.46e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0139129 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0268768 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.9e+07s, dt:98428.4s, Cycle: 560 +well_1Control: BHP (at the specified reference elevation): 25504765.5136409 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 3.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.77e-04 ) ; ( Rwell ) = ( 6.21e-12 ) ; ( R ) = ( 6.77e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0225786 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0449005 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.50689e+07, 1.51081e+07, 1.51471e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.56552e+06, 2.64375e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.63 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.76346, 726.867 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1331.1, 703040 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 332.259, 212014 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 998.842, 491026 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 35.373, 0.0676116 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1295.73, 703040 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1331.1, 0 }, { 705.557, 702320 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.50177e+07, 1.5053e+07, 1.50875e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.51441e+06, 2.58419e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.22 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 223.22 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 215848 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64754.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151093 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215848 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 6.38277, 215841 } } kg +well_1Control: BHP (at the specified reference elevation): 25511387.04077764 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 1.60152 +compflowStatistics: Max component CFL number: 48.2349 +Time: 6.90984e+07s, dt:129348s, Cycle: 561 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 5.93e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 7.09e-09 ) ; ( R ) = ( 5.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0573786 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.92278e+07s, dt:147021s, Cycle: 562 +well_1Control: BHP (at the specified reference elevation): 25520029.045241185 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 6.60e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 7.49e-10 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 7.53e-14 ) ; ( R ) = ( 4.90e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25529885.370665114 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0336773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619873 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.93748e+07s, dt:159167s, Cycle: 563 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 3.23e-09 ) ; ( R ) = ( 5.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 3.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 8.71e-10 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.43e-15 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-06 ) ; ( Rwell ) = ( 1.28e-14 ) ; ( R ) = ( 2.18e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0364066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0756491 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.9534e+07s, dt:151041s, Cycle: 564 +well_1Control: BHP (at the specified reference elevation): 25540554.941174142 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 5.90e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 8.79e-13 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-06 ) ; ( Rwell ) = ( 3.25e-15 ) ; ( R ) = ( 2.54e-06 ) ; + Last LinSolve(iter,res) = ( 8, 2.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.034488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666153 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.9685e+07s, dt:156072s, Cycle: 565 +well_1Control: BHP (at the specified reference elevation): 25550666.20269196 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; ( R ) = ( 4.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 8.14e-10 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.81e-03 ) ; ( Rwell ) = ( 2.13e-10 ) ; ( R ) = ( 8.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.88e-05 ) ; ( Rwell ) = ( 2.46e-14 ) ; ( R ) = ( 3.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0354319 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678134 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.98411e+07s, dt:158923s, Cycle: 566 +well_1Control: BHP (at the specified reference elevation): 25561064.86770024 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 8.57e-10 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 2.18e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.68e-05 ) ; ( Rwell ) = ( 4.30e-14 ) ; ( R ) = ( 3.68e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0361845 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0739869 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7e+07s, dt:153109s, Cycle: 567 +well_1Control: BHP (at the specified reference elevation): 25571643.972053498 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 2.95e-09 ) ; ( R ) = ( 4.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.31e-03 ) ; ( Rwell ) = ( 1.42e-12 ) ; ( R ) = ( 4.31e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-05 ) ; ( Rwell ) = ( 5.95e-15 ) ; ( R ) = ( 1.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0348798 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696738 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.51044e+07, 1.51437e+07, 1.51826e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.59926e+06, 2.67748e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.656 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.81636, 726.84 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1354.34, 703034 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 336.268, 212028 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1018.07, 491006 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 36.4884, 0.0676148 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1317.85, 703034 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1354.34, 0 }, { 712.232, 702307 } } kg +well_1Control: BHP (at the specified reference elevation): 25581863.698894687 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.50533e+07, 1.50885e+07, 1.51231e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.54813e+06, 2.61793e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.228 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.16947e-06, 223.228 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.000414127, 215861 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.000414127, 64758.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { -5.42101e-20, 151103 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.000414127, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215861 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.000414127, 0 }, { 7.65341, 215854 } } kg +compflowStatistics: Max phase CFL number: 54.9751 +compflowStatistics: Max component CFL number: 74.7833 +Time: 7.01531e+07s, dt:153586s, Cycle: 568 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 1.60e-12 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-05 ) ; ( Rwell ) = ( 3.08e-16 ) ; ( R ) = ( 1.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0351154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641883 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.03067e+07s, dt:162585s, Cycle: 569 +well_1Control: BHP (at the specified reference elevation): 25592111.70859921 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 9.01e-10 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.50e-04 ) ; ( Rwell ) = ( 6.55e-14 ) ; ( R ) = ( 3.50e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0372178 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0751024 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.04693e+07s, dt:155051s, Cycle: 570 +well_1Control: BHP (at the specified reference elevation): 25602988.943836283 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 1.36e-12 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-06 ) ; ( Rwell ) = ( 7.63e-15 ) ; ( R ) = ( 2.12e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0354802 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695214 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.06243e+07s, dt:155761s, Cycle: 571 +well_1Control: BHP (at the specified reference elevation): 25613405.556157142 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 8.10e-10 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-04 ) ; ( Rwell ) = ( 4.31e-14 ) ; ( R ) = ( 1.83e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0354635 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688217 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.07801e+07s, dt:157528s, Cycle: 572 +well_1Control: BHP (at the specified reference elevation): 25623824.675505225 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 3.07e-09 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 8.33e-10 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.56e-04 ) ; ( Rwell ) = ( 3.08e-14 ) ; ( R ) = ( 9.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0359106 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629896 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.09376e+07s, dt:62379.5s, Cycle: 573 +well_1Control: BHP (at the specified reference elevation): 25634377.6124148 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 1.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 5.56e-10 ) ; ( R ) = ( 9.81e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.04e-05 ) ; ( Rwell ) = ( 4.61e-14 ) ; ( R ) = ( 6.04e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.015055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0286716 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.1e+07s, dt:102869s, Cycle: 574 +well_1Control: BHP (at the specified reference elevation): 25638608.203240335 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 5.94e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.33e-09 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.46e-04 ) ; ( Rwell ) = ( 4.53e-13 ) ; ( R ) = ( 4.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0238398 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0470006 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 25645510.94660531 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.51365e+07, 1.51758e+07, 1.52147e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.63304e+06, 2.71125e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.679 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.86431, 726.815 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1375.5, 703029 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 339.742, 212040 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1035.76, 490988 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 37.5077, 0.0676178 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1337.99, 703029 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1375.5, 0 }, { 717.891, 702296 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.50853e+07, 1.51206e+07, 1.51552e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.58184e+06, 2.6517e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.235 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 6.73798e-06, 223.235 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.00239333, 215874 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.00239333, 64762.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151112 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.00239333, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215874 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.00239333, 0 }, { 8.91319, 215865 } } kg +compflowStatistics: Max phase CFL number: 36.8227 +compflowStatistics: Max component CFL number: 50.0951 +Time: 7.11029e+07s, dt:131722s, Cycle: 575 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 2.16e-09 ) ; ( R ) = ( 3.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 5.04e-13 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.14e-06 ) ; ( Rwell ) = ( 4.70e-15 ) ; ( R ) = ( 5.14e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0298775 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0582212 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.12346e+07s, dt:148365s, Cycle: 576 +well_1Control: BHP (at the specified reference elevation): 25654292.151534453 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 1.76e-12 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-06 ) ; ( Rwell ) = ( 3.83e-15 ) ; ( R ) = ( 2.51e-06 ) ; + Last LinSolve(iter,res) = ( 8, 9.73e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0339381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644799 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.1383e+07s, dt:156598s, Cycle: 577 +well_1Control: BHP (at the specified reference elevation): 25664195.58671529 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 3.02e-09 ) ; ( R ) = ( 6.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 7.94e-10 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.41e-04 ) ; ( Rwell ) = ( 9.44e-14 ) ; ( R ) = ( 3.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0355175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0713677 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.15396e+07s, dt:154584s, Cycle: 578 +well_1Control: BHP (at the specified reference elevation): 25674604.937974982 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 7.91e-10 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-04 ) ; ( Rwell ) = ( 4.79e-14 ) ; ( R ) = ( 1.17e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.40e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25684961.717097677 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0354141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06697 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.16941e+07s, dt:159178s, Cycle: 579 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.15e-09 ) ; ( R ) = ( 4.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 1.17e-12 ) ; ( R ) = ( 2.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.12e-06 ) ; ( Rwell ) = ( 3.85e-15 ) ; ( R ) = ( 2.12e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0364323 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681579 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.18533e+07s, dt:146684s, Cycle: 580 +well_1Control: BHP (at the specified reference elevation): 25695635.775014784 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 7.07e-10 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.41e-05 ) ; ( Rwell ) = ( 3.30e-14 ) ; ( R ) = ( 9.41e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0335522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0620194 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.2e+07s, dt:158750s, Cycle: 581 +well_1Control: BHP (at the specified reference elevation): 25705479.97306584 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 2.97e-13 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0360002 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697722 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.51721e+07, 1.52114e+07, 1.52503e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.66677e+06, 2.74498e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.705 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.91758, 726.788 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1399.12, 703023 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 343.494, 212054 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1055.62, 490969 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 38.7537, 0.0676207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1360.36, 703022 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1399.12, 0 }, { 723.965, 702284 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.51209e+07, 1.51562e+07, 1.51908e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.61559e+06, 2.68544e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.243 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 2.4229e-05, 223.243 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.0086353, 215888 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.0086353, 64766.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151121 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.0086353, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215888 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.0086353, 0 }, { 10.4361, 215877 } } kg +well_1Control: BHP (at the specified reference elevation): 25716101.692422673 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 56.633 +compflowStatistics: Max component CFL number: 77.0533 +Time: 7.21587e+07s, dt:159095s, Cycle: 582 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 5.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 8.29e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 3.54e-14 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.27e-06 ) ; ( Rwell ) = ( 3.49e-15 ) ; ( R ) = ( 5.27e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0362382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658713 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.23178e+07s, dt:165607s, Cycle: 583 +well_1Control: BHP (at the specified reference elevation): 25726743.600560293 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 5.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 9.01e-10 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 1.84e-15 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0378477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695114 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.24835e+07s, dt:166381s, Cycle: 584 +well_1Control: BHP (at the specified reference elevation): 25737855.761540655 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 9.07e-10 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-04 ) ; ( Rwell ) = ( 7.65e-14 ) ; ( R ) = ( 2.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0381033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0720732 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.26498e+07s, dt:163159s, Cycle: 585 +well_1Control: BHP (at the specified reference elevation): 25749049.831331454 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.25e-09 ) ; ( R ) = ( 4.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.08e-12 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-05 ) ; ( Rwell ) = ( 3.17e-15 ) ; ( R ) = ( 1.29e-05 ) ; + Last LinSolve(iter,res) = ( 8, 1.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0370343 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695631 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.2813e+07s, dt:163841s, Cycle: 586 +well_1Control: BHP (at the specified reference elevation): 25759974.58216013 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 4.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 8.61e-10 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.97e-04 ) ; ( Rwell ) = ( 1.39e-13 ) ; ( R ) = ( 2.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0372071 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683457 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.29768e+07s, dt:23167.9s, Cycle: 587 +well_1Control: BHP (at the specified reference elevation): 25770905.842738904 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.55e-03 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 1.21e-10 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e-05 ) ; ( Rwell ) = ( 3.90e-14 ) ; ( R ) = ( 2.46e-05 ) ; + Last LinSolve(iter,res) = ( 10, 5.73e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25772477.502925724 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00619472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00959672 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.3e+07s, dt:46335.8s, Cycle: 588 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; ( R ) = ( 1.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 2.94e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.34e-04 ) ; ( Rwell ) = ( 1.87e-13 ) ; ( R ) = ( 3.34e-04 ) ; + Last LinSolve(iter,res) = ( 9, 6.15e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25775621.215811722 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.01097 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.019048 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.52022e+07, 1.52414e+07, 1.52804e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.70057e+06, 2.77877e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.727 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.96267, 726.765 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1419.19, 703017 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 346.543, 212066 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1072.65, 490952 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 39.9348, 0.067623 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1379.26, 703017 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1419.19, 0 }, { 728.745, 702274 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.51509e+07, 1.51863e+07, 1.52208e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.64936e+06, 2.71924e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.25 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 5.38571e-05, 223.25 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.0192495, 215899 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.0192495, 64769.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 3.46945e-18, 151129 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.0192495, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215899 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.0192495, 0 }, { 11.8119, 215887 } } kg +compflowStatistics: Max phase CFL number: 16.4829 +compflowStatistics: Max component CFL number: 22.4281 +Time: 7.30463e+07s, dt:90017.4s, Cycle: 589 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 5.91e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 9.91e-10 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-04 ) ; ( Rwell ) = ( 3.56e-13 ) ; ( R ) = ( 1.61e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.021016 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0383184 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.31364e+07s, dt:128915s, Cycle: 590 +well_1Control: BHP (at the specified reference elevation): 25781697.8703503 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.83e-03 ) ; ( Rwell ) = ( 3.64e-13 ) ; ( R ) = ( 1.83e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-06 ) ; ( Rwell ) = ( 1.89e-15 ) ; ( R ) = ( 2.14e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.029522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557949 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.32653e+07s, dt:149084s, Cycle: 591 +well_1Control: BHP (at the specified reference elevation): 25790337.64676205 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 5.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 7.22e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.05e-04 ) ; ( Rwell ) = ( 9.14e-14 ) ; ( R ) = ( 9.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0338012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633796 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.34144e+07s, dt:159116s, Cycle: 592 +well_1Control: BHP (at the specified reference elevation): 25800332.12366966 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.05e-09 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 7.97e-10 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 7.75e-14 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-06 ) ; ( Rwell ) = ( 2.32e-16 ) ; ( R ) = ( 1.57e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0360767 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659293 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.35735e+07s, dt:165534s, Cycle: 593 +well_1Control: BHP (at the specified reference elevation): 25810969.95403616 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 8.66e-10 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 2.55e-15 ) ; ( R ) = ( 4.90e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0376572 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688801 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.3739e+07s, dt:167318s, Cycle: 594 +well_1Control: BHP (at the specified reference elevation): 25822052.43313898 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 3.32e-09 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 8.84e-10 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.96e-04 ) ; ( Rwell ) = ( 5.46e-14 ) ; ( R ) = ( 1.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0379962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684055 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.39063e+07s, dt:93679s, Cycle: 595 +well_1Control: BHP (at the specified reference elevation): 25833249.7949442 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 3.70e-13 ) ; ( R ) = ( 4.31e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0218915 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0387046 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.4e+07s, dt:133456s, Cycle: 596 +well_1Control: BHP (at the specified reference elevation): 25839575.899872065 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 3.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 5.53e-10 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-04 ) ; ( Rwell ) = ( 4.32e-14 ) ; ( R ) = ( 1.02e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0303027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0535201 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.52389e+07, 1.52782e+07, 1.53171e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.73442e+06, 2.81262e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.754 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.01802, 726.736 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1443.95, 703010 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 350.157, 212080 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1093.8, 490931 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 41.2357, 0.0676264 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1402.72, 703010 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1443.95, 0 }, { 734.309, 702261 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.51877e+07, 1.5223e+07, 1.52576e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.68317e+06, 2.75309e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.258 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00011419, 223.258 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.0409555, 215914 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.0409555, 64774.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151139 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.0409555, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215914 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.0409555, 0 }, { 13.6083, 215900 } } kg +well_1Control: BHP (at the specified reference elevation): 25848522.467836604 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 47.3088 +compflowStatistics: Max component CFL number: 64.3789 +Time: 7.41335e+07s, dt:158301s, Cycle: 597 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 5.82e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.86e-09 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 7.73e-10 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 6.65e-14 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.19e-06 ) ; ( Rwell ) = ( 1.42e-15 ) ; ( R ) = ( 2.19e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0357406 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.42918e+07s, dt:170621s, Cycle: 598 +well_1Control: BHP (at the specified reference elevation): 25859044.23212914 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 9.25e-10 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-04 ) ; ( Rwell ) = ( 2.19e-13 ) ; ( R ) = ( 2.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.98e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25870492.8275055 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0387059 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701634 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.44624e+07s, dt:170356s, Cycle: 599 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; ( R ) = ( 4.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 9.02e-10 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.55e-04 ) ; ( Rwell ) = ( 7.24e-14 ) ; ( R ) = ( 4.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.36e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25881906.241195925 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0384808 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685837 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.46327e+07s, dt:172685s, Cycle: 600 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 3.47e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 9.20e-10 ) ; ( R ) = ( 2.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 2.40e-10 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 7.65e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.95e-03 ) ; ( Rwell ) = ( 6.19e-11 ) ; ( R ) = ( 7.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.52e-05 ) ; ( Rwell ) = ( 1.61e-14 ) ; ( R ) = ( 5.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0391073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644337 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.48054e+07s, dt:182352s, Cycle: 601 +well_1Control: BHP (at the specified reference elevation): 25893467.358772174 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.80e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.03e-09 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 9.11e-10 ) ; ( R ) = ( 2.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 8.01e-10 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.99e-04 ) ; ( Rwell ) = ( 1.86e-14 ) ; ( R ) = ( 1.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0413043 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0719566 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.49878e+07s, dt:12227.7s, Cycle: 602 +well_1Control: BHP (at the specified reference elevation): 25905712.474731993 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 3.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 5.52e-11 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.90e-06 ) ; ( Rwell ) = ( 2.76e-14 ) ; ( R ) = ( 5.90e-06 ) ; + Last LinSolve(iter,res) = ( 9, 6.59e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25906543.490398727 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0037054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00484721 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 7.5e+07s, dt:24455.4s, Cycle: 603 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.53e-03 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 6.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-03 ) ; ( Rwell ) = ( 8.80e-11 ) ; ( R ) = ( 3.62e-03 ) ; + Last LinSolve(iter,res) = ( 3, 8.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.56e-06 ) ; ( Rwell ) = ( 5.90e-14 ) ; ( R ) = ( 6.56e-06 ) ; + Last LinSolve(iter,res) = ( 9, 8.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00572003 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00969941 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.5269e+07, 1.53083e+07, 1.53472e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.76821e+06, 2.8464e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.776 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.06341, 726.712 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1464.35, 703005 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 353.079, 212091 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1111.28, 490913 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 42.2956, 0.338536 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1422.06, 703004 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1464.35, 0 }, { 738.668, 702251 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.52178e+07, 1.52532e+07, 1.52877e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.71698e+06, 2.78687e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.265 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.000187845, 223.264 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.0675634, 215925 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.0675634, 64777.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151148 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.0675634, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215925 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.0675634, 0 }, { 15.1669, 215910 } } kg +well_1Control: BHP (at the specified reference elevation): 25908209.65202333 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 8.64459 +compflowStatistics: Max component CFL number: 11.7646 +Time: 7.50245e+07s, dt:48910.7s, Cycle: 604 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 1.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 3.05e-10 ) ; ( R ) = ( 6.32e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 4.42e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 2.31e-10 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.31e-10 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.06e-02 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 1.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.96e-03 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 9.96e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.38e-05 ) ; ( Rwell ) = ( 7.68e-14 ) ; ( R ) = ( 2.38e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0117932 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0193504 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.50734e+07s, dt:94491.1s, Cycle: 605 +well_1Control: BHP (at the specified reference elevation): 25911521.716779403 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 2.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-04 ) ; ( Rwell ) = ( 5.84e-13 ) ; ( R ) = ( 1.98e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.32e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 25917848.75499525 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0215843 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0374695 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.51679e+07s, dt:136907s, Cycle: 606 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 2.12e-09 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.66e-13 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-04 ) ; ( Rwell ) = ( 4.71e-15 ) ; ( R ) = ( 1.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 2.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0308455 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0537581 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.53048e+07s, dt:161959s, Cycle: 607 +well_1Control: BHP (at the specified reference elevation): 25926940.959748123 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 8.05e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-04 ) ; ( Rwell ) = ( 1.35e-13 ) ; ( R ) = ( 2.58e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0365925 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0614009 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.54667e+07s, dt:176406s, Cycle: 608 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 4.59e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 25937747.730888817 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 3.59e-09 ) ; ( R ) = ( 5.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 9.63e-10 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.63e-04 ) ; ( Rwell ) = ( 3.06e-14 ) ; ( R ) = ( 7.63e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0400266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689134 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.56431e+07s, dt:178251s, Cycle: 609 +well_1Control: BHP (at the specified reference elevation): 25949616.010471873 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 9.56e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-04 ) ; ( Rwell ) = ( 5.96e-14 ) ; ( R ) = ( 1.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.040271 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683804 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.58214e+07s, dt:178619s, Cycle: 610 +well_1Control: BHP (at the specified reference elevation): 25961563.204850964 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.57e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 9.55e-10 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.62e-04 ) ; ( Rwell ) = ( 1.78e-13 ) ; ( R ) = ( 5.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0400242 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645172 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.6e+07s, dt:188460s, Cycle: 611 +well_1Control: BHP (at the specified reference elevation): 25973463.412480388 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.74e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-04 ) ; ( Rwell ) = ( 6.72e-14 ) ; ( R ) = ( 3.10e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0423141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696678 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.53083e+07, 1.53476e+07, 1.53865e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.80197e+06, 2.88016e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.804 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.12266, 726.682 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1491.12, 702997 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 356.688, 212107 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1134.43, 490891 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 43.8279, 0.338543 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1447.29, 702997 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1491.12, 0 }, { 744.128, 702238 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.52571e+07, 1.52925e+07, 1.5327e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.75078e+06, 2.82064e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.273 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.000321243, 223.273 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.115969, 215940 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.115969, 64782.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151158 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.115969, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215940 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.115969, 0 }, { 17.3125, 215923 } } kg +well_1Control: BHP (at the specified reference elevation): 25986038.740236104 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 66.372 +compflowStatistics: Max component CFL number: 90.3353 +Time: 7.61885e+07s, dt:189058s, Cycle: 612 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 4.04e-09 ) ; ( R ) = ( 5.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 6.61e-14 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0424627 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0705335 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.63775e+07s, dt:188102s, Cycle: 613 +well_1Control: BHP (at the specified reference elevation): 25998659.245431535 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 5.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.06e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 4.13e-14 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-06 ) ; ( Rwell ) = ( 4.27e-15 ) ; ( R ) = ( 1.16e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0422824 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690995 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.65656e+07s, dt:189730s, Cycle: 614 +well_1Control: BHP (at the specified reference elevation): 26011238.21845958 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 6.44e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.22e-03 ) ; ( Rwell ) = ( 5.92e-12 ) ; ( R ) = ( 2.22e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.22e-05 ) ; ( Rwell ) = ( 1.67e-16 ) ; ( R ) = ( 6.22e-05 ) ; + Last LinSolve(iter,res) = ( 7, 2.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0424231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.67554e+07s, dt:193429s, Cycle: 615 +well_1Control: BHP (at the specified reference elevation): 26023884.93792098 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 5.73e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 4.15e-09 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 2.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.71e-04 ) ; ( Rwell ) = ( 1.17e-14 ) ; ( R ) = ( 3.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0434751 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0700176 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.69488e+07s, dt:51220.4s, Cycle: 616 +well_1Control: BHP (at the specified reference elevation): 26036849.398668297 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 1.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.78e-03 ) ; ( Rwell ) = ( 3.48e-10 ) ; ( R ) = ( 6.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 4.65e-14 ) ; ( R ) = ( 6.20e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0123492 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0186693 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.7e+07s, dt:100209s, Cycle: 617 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: BHP (at the specified reference elevation): 26040343.62553204 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 5.86e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.39e-13 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.68e-06 ) ; ( Rwell ) = ( 5.79e-15 ) ; ( R ) = ( 3.68e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.18e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26047142.717838537 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0230545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.036563 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.53392e+07, 1.53784e+07, 1.54173e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.83572e+06, 2.9139e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.827 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.16932, 726.657 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1512.29, 702991 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 359.465, 212119 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1152.82, 490873 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 44.9997, 0.338551 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1467.29, 702991 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1512.29, 0 }, { 748.099, 702228 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.52879e+07, 1.53233e+07, 1.53578e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.78453e+06, 2.85439e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.28 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.000458274, 223.28 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.165915, 215952 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.165915, 64785.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151167 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.165915, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215952 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.165915, 0 }, { 19.0765, 215933 } } kg +compflowStatistics: Max phase CFL number: 35.1898 +compflowStatistics: Max component CFL number: 47.8986 +Time: 7.71002e+07s, dt:147030s, Cycle: 618 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 5.83e-08 ) ; ( R ) = ( 3.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 2.43e-09 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 6.32e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.42e-04 ) ; ( Rwell ) = ( 3.83e-14 ) ; ( R ) = ( 2.42e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0332422 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0521612 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.72472e+07s, dt:177122s, Cycle: 619 +well_1Control: BHP (at the specified reference elevation): 26056987.35694915 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 5.75e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.42e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 9.10e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 2.38e-10 ) ; ( R ) = ( 9.19e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.27e-05 ) ; ( Rwell ) = ( 8.71e-14 ) ; ( R ) = ( 7.27e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0395804 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629459 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.74244e+07s, dt:189879s, Cycle: 620 +well_1Control: BHP (at the specified reference elevation): 26068771.359517477 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.90e-09 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 9.50e-15 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26081356.045618664 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0421811 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678791 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.76142e+07s, dt:193793s, Cycle: 621 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 4.04e-09 ) ; ( R ) = ( 7.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.54e-04 ) ; ( Rwell ) = ( 1.82e-14 ) ; ( R ) = ( 3.54e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0433058 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676605 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.7808e+07s, dt:191966s, Cycle: 622 +well_1Control: BHP (at the specified reference elevation): 26094268.87882369 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 4.04e-09 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 2.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-04 ) ; ( Rwell ) = ( 7.96e-14 ) ; ( R ) = ( 1.70e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0429499 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657129 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.8e+07s, dt:200138s, Cycle: 623 +well_1Control: BHP (at the specified reference elevation): 26107079.894231312 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 5.72e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 4.89e-08 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 6.62e-10 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 8.24e-14 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.09e-06 ) ; ( Rwell ) = ( 7.35e-15 ) ; ( R ) = ( 3.09e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0445357 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683218 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.53761e+07, 1.54154e+07, 1.54543e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.8694e+06, 2.94758e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.854 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.22522, 726.628 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1537.78, 702984 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 362.588, 212133 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1175.2, 490851 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 46.3988, 0.338561 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1491.38, 702984 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1537.78, 0 }, { 752.834, 702216 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.5325e+07, 1.53603e+07, 1.53948e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.81829e+06, 2.88807e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.288 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.000667303, 223.288 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.242424, 215967 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.242424, 64790.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151177 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.242424, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215967 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.242424, 0 }, { 21.2914, 215945 } } kg +well_1Control: BHP (at the specified reference elevation): 26120421.96831329 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 70.0389 +compflowStatistics: Max component CFL number: 95.343 +Time: 7.82001e+07s, dt:203389s, Cycle: 624 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 1.60e-14 ) ; ( R ) = ( 4.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0452089 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695314 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.84035e+07s, dt:204301s, Cycle: 625 +well_1Control: BHP (at the specified reference elevation): 26133921.23190054 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 4.42e-09 ) ; ( R ) = ( 6.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 1.05e-09 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 9.27e-10 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 8.18e-10 ) ; ( R ) = ( 3.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 7.17e-10 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 6.32e-10 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 5.58e-10 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 4.89e-10 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.88e-05 ) ; ( Rwell ) = ( 2.38e-16 ) ; ( R ) = ( 9.88e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0455956 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681619 +Time: 7.86078e+07s, dt:204301s, Cycle: 626 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 5.69e-08 ) ; ( R ) = ( 4.60e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 26147522.914550304 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 4.48e-09 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-04 ) ; ( Rwell ) = ( 5.95e-15 ) ; ( R ) = ( 6.55e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0457022 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673553 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.88121e+07s, dt:187872s, Cycle: 627 +well_1Control: BHP (at the specified reference elevation): 26161198.167288087 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 5.72e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.82e-09 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 9.96e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-04 ) ; ( Rwell ) = ( 6.45e-17 ) ; ( R ) = ( 1.82e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0420321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633044 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.9e+07s, dt:200668s, Cycle: 628 +well_1Control: BHP (at the specified reference elevation): 26173762.427460093 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 5.71e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 4.30e-09 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 2.71e-13 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.48e-06 ) ; ( Rwell ) = ( 9.10e-15 ) ; ( R ) = ( 1.48e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0444188 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662329 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.54098e+07, 1.5449e+07, 1.54879e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.90306e+06, 2.98123e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.878 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.27611, 726.602 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1561.12, 702977 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 365.369, 212146 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1195.75, 490832 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 47.7145, 0.33857 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1513.4, 702977 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1561.12, 0 }, { 756.909, 702205 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.53587e+07, 1.5394e+07, 1.54284e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.85196e+06, 2.92173e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.296 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.000909528, 223.295 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.331454, 215980 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.331454, 64794.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151186 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.331454, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215980 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.331454, 0 }, { 23.3779, 215956 } } kg +well_1Control: BHP (at the specified reference elevation): 26187060.195404842 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 70.0047 +compflowStatistics: Max component CFL number: 95.3051 +Time: 7.92007e+07s, dt:208135s, Cycle: 629 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 5.65e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 4.51e-09 ) ; ( R ) = ( 5.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.41e-04 ) ; ( Rwell ) = ( 6.36e-14 ) ; ( R ) = ( 9.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0460526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674461 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.94088e+07s, dt:213324s, Cycle: 630 +well_1Control: BHP (at the specified reference elevation): 26200831.049198397 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.62e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; ( R ) = ( 8.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.69e-04 ) ; ( Rwell ) = ( 1.75e-12 ) ; ( R ) = ( 4.69e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0474009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692391 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.96221e+07s, dt:214881s, Cycle: 631 +well_1Control: BHP (at the specified reference elevation): 26215043.100048482 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 4.80e-09 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.51e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.48e-04 ) ; ( Rwell ) = ( 1.20e-13 ) ; ( R ) = ( 2.48e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.77e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26229245.328295566 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0473023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069064 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.9837e+07s, dt:162991s, Cycle: 632 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; ( R ) = ( 3.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.75e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 7.31e-10 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-04 ) ; ( Rwell ) = ( 7.85e-14 ) ; ( R ) = ( 3.26e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0362132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051965 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8e+07s, dt:196793s, Cycle: 633 +well_1Control: BHP (at the specified reference elevation): 26240047.977755226 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 3.92e-09 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 6.24e-13 ) ; ( R ) = ( 2.41e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.98e-05 ) ; ( Rwell ) = ( 7.92e-16 ) ; ( R ) = ( 8.98e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0434585 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621915 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.54431e+07, 1.54824e+07, 1.55213e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.93652e+06, 3.01469e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.902 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.32645, 726.576 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1584.31, 702971 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 368.071, 212159 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1216.24, 490812 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 49.1016, 0.338578 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1535.21, 702970 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1584.31, 0 }, { 760.93, 702194 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.53922e+07, 1.54274e+07, 1.54618e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.88557e+06, 2.95519e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.303 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00121569, 223.302 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.444393, 215993 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.444393, 64798.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151194 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.444393, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 215993 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.444393, 0 }, { 25.5018, 215967 } } kg +well_1Control: BHP (at the specified reference elevation): 26253075.010344148 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 68.4409 +compflowStatistics: Max component CFL number: 93.1836 +Time: 8.01968e+07s, dt:212604s, Cycle: 634 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 5.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.22e-04 ) ; ( Rwell ) = ( 1.57e-13 ) ; ( R ) = ( 4.22e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.91e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26267166.653471857 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0468551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681852 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.04094e+07s, dt:216343s, Cycle: 635 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 5.63e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.78e-09 ) ; ( R ) = ( 4.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.14e-09 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 9.98e-10 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 8.80e-10 ) ; ( R ) = ( 3.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.12e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 7.72e-10 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 6.79e-10 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.00e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 5.96e-10 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 4.77e-14 ) ; ( R ) = ( 4.96e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0478252 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683114 +Time: 8.06257e+07s, dt:216343s, Cycle: 636 +well_1Control: BHP (at the specified reference elevation): 26281525.749875255 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 4.79e-09 ) ; ( R ) = ( 5.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.25e-09 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 2.57e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.11e-09 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 5.57e-18 ) ; ( R ) = ( 6.33e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0475715 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066907 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.08421e+07s, dt:157918s, Cycle: 637 +well_1Control: BHP (at the specified reference elevation): 26295838.633858517 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.62e-08 ) ; ( R ) = ( 3.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 2.58e-09 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 6.75e-10 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 1.14e-13 ) ; ( R ) = ( 4.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0351463 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0488297 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.1e+07s, dt:197798s, Cycle: 638 +well_1Control: BHP (at the specified reference elevation): 26306336.59248996 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 5.64e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.85e-04 ) ; ( Rwell ) = ( 1.15e-13 ) ; ( R ) = ( 2.85e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.08e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26319445.425788805 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0436725 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624392 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.54766e+07, 1.55159e+07, 1.55548e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 2.96999e+06, 3.04816e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.927 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.37712, 726.55 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1607.77, 702964 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 370.809, 212171 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1236.96, 490793 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 50.4894, 0.338586 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1557.28, 702964 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1607.77, 0 }, { 764.753, 702184 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.54257e+07, 1.54609e+07, 1.54953e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.91908e+06, 2.98866e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.311 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00159775, 223.309 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.585857, 216005 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.585857, 64802.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151203 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.585857, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216005 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.585857, 0 }, { 27.6771, 215977 } } kg +compflowStatistics: Max phase CFL number: 68.5776 +compflowStatistics: Max component CFL number: 93.3772 +Time: 8.11978e+07s, dt:213146s, Cycle: 639 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 5.62e-08 ) ; ( R ) = ( 4.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 4.57e-09 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-04 ) ; ( Rwell ) = ( 8.82e-14 ) ; ( R ) = ( 2.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.18e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26333538.056663617 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0468062 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654502 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.14109e+07s, dt:222801s, Cycle: 640 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 5.60e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 4.86e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.65e-03 ) ; ( Rwell ) = ( 3.27e-10 ) ; ( R ) = ( 9.65e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.03e-05 ) ; ( Rwell ) = ( 4.79e-14 ) ; ( R ) = ( 8.03e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0484051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676666 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.16337e+07s, dt:227865s, Cycle: 641 +well_1Control: BHP (at the specified reference elevation): 26348134.24790712 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 5.07e-09 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.37e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.41e-04 ) ; ( Rwell ) = ( 1.02e-14 ) ; ( R ) = ( 4.41e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0498915 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689862 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.18616e+07s, dt:138390s, Cycle: 642 +well_1Control: BHP (at the specified reference elevation): 26363171.00580126 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 5.58e-08 ) ; ( R ) = ( 2.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.96e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.37e-03 ) ; ( Rwell ) = ( 2.05e-13 ) ; ( R ) = ( 2.37e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 2.49e-15 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0307634 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0424035 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.2e+07s, dt:187730s, Cycle: 643 +well_1Control: BHP (at the specified reference elevation): 26372352.090654667 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 5.61e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 9.13e-10 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 5.89e-14 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0410345 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561041 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.55096e+07, 1.55488e+07, 1.55877e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.00333e+06, 3.08149e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.951 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.42683, 726.524 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1630.9, 702958 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 373.373, 212184 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1257.53, 490773 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 51.8954, 0.338596 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1579.01, 702957 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1630.9, 0 }, { 768.537, 702173 } } kg +well_1Control: BHP (at the specified reference elevation): 26384707.876091994 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.54588e+07, 1.54939e+07, 1.55282e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.95252e+06, 3.022e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.318 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00205352, 223.316 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.755255, 216018 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.755255, 64806 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { -1.11022e-16, 151212 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.755255, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216018 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.755255, 0 }, { 29.8573, 215988 } } kg +compflowStatistics: Max phase CFL number: 64.8893 +compflowStatistics: Max component CFL number: 88.3625 +Time: 8.21877e+07s, dt:216364s, Cycle: 644 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 5.56e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.54e-09 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 3.10e-10 ) ; ( R ) = ( 9.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.44e-05 ) ; ( Rwell ) = ( 1.11e-14 ) ; ( R ) = ( 6.44e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.047085 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645039 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.24041e+07s, dt:228314s, Cycle: 645 +well_1Control: BHP (at the specified reference elevation): 26398926.6069728 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 5.55e-08 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-04 ) ; ( Rwell ) = ( 6.38e-12 ) ; ( R ) = ( 2.98e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0499026 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674398 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.26324e+07s, dt:234021s, Cycle: 646 +well_1Control: BHP (at the specified reference elevation): 26414005.7574898 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 5.57e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 5.35e-09 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 1.23e-14 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.80e-05 ) ; ( Rwell ) = ( 1.00e-15 ) ; ( R ) = ( 2.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0510053 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682815 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.28664e+07s, dt:133572s, Cycle: 647 +well_1Control: BHP (at the specified reference elevation): 26429423.240604877 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 5.56e-08 ) ; ( R ) = ( 2.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.93e-04 ) ; ( Rwell ) = ( 3.39e-13 ) ; ( R ) = ( 3.93e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.73e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26438248.245599743 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.029559 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0389014 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.3e+07s, dt:189781s, Cycle: 648 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.57e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.46e-09 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 9.04e-10 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.16e-13 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.21e-05 ) ; ( Rwell ) = ( 8.06e-15 ) ; ( R ) = ( 3.21e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.00e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26450731.591948368 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0413779 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0549825 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.55429e+07, 1.55822e+07, 1.56211e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.03661e+06, 3.11477e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.975 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.47714, 726.498 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1654.43, 702951 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 376.022, 212197 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1278.41, 490754 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 53.2939, 0.338604 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1601.14, 702951 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1654.43, 0 }, { 772.201, 702163 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.54922e+07, 1.55272e+07, 1.55616e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 2.98586e+06, 3.05528e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.325 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00259966, 223.323 } rm^3 +compflowStatistics, caprock: Phase mass: { 0.959038, 216031 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0.959038, 64809.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151221 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0.959038, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216031 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0.959038, 0 }, { 32.0907, 215998 } } kg +compflowStatistics: Max phase CFL number: 65.3976 +compflowStatistics: Max component CFL number: 89.0616 +Time: 8.31898e+07s, dt:221454s, Cycle: 649 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 5.54e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 4.68e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 1.23e-09 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 3.13e-10 ) ; ( R ) = ( 9.92e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-04 ) ; ( Rwell ) = ( 2.73e-14 ) ; ( R ) = ( 1.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0479856 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645279 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.34112e+07s, dt:233630s, Cycle: 650 +well_1Control: BHP (at the specified reference elevation): 26465260.637386605 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 5.52e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 5.16e-09 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 7.77e-10 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.96e-04 ) ; ( Rwell ) = ( 2.58e-14 ) ; ( R ) = ( 4.96e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0506785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0677818 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.36449e+07s, dt:238672s, Cycle: 651 +well_1Control: BHP (at the specified reference elevation): 26480614.317404263 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 5.53e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 5.39e-09 ) ; ( R ) = ( 8.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.70e-04 ) ; ( Rwell ) = ( 1.09e-13 ) ; ( R ) = ( 6.70e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0516431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067315 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.38835e+07s, dt:116464s, Cycle: 652 +well_1Control: BHP (at the specified reference elevation): 26496257.787567236 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; ( R ) = ( 2.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.83e-04 ) ; ( Rwell ) = ( 9.93e-14 ) ; ( R ) = ( 8.83e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.025719 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0328613 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.4e+07s, dt:180202s, Cycle: 653 +well_1Control: BHP (at the specified reference elevation): 26503913.221115053 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 5.52e-08 ) ; ( R ) = ( 3.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 8.10e-10 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.18e-04 ) ; ( Rwell ) = ( 9.12e-14 ) ; ( R ) = ( 3.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.039073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0510628 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 26515712.878599606 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.55757e+07, 1.5615e+07, 1.56539e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.06978e+06, 3.14793e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 730.999 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.52657, 726.472 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1677.66, 702945 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 378.493, 212209 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1299.17, 490735 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 54.7043, 0.338612 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1622.96, 702944 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1677.66, 0 }, { 775.794, 702153 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.55251e+07, 1.55601e+07, 1.55944e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.01914e+06, 3.08845e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.333 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00322774, 223.329 } rm^3 +compflowStatistics, caprock: Phase mass: { 1.19431, 216043 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 1.19431, 64813.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { -2.22045e-16, 151229 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 1.19431, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216043 } kg +compflowStatistics, caprock: Dissolved component mass: { { 1.19431, 0 }, { 34.3147, 216008 } } kg +compflowStatistics: Max phase CFL number: 61.9106 +compflowStatistics: Max component CFL number: 84.3195 +Time: 8.41802e+07s, dt:219854s, Cycle: 654 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 5.50e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.49e-09 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 3.07e-10 ) ; ( R ) = ( 8.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 6.73e-14 ) ; ( R ) = ( 7.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0475928 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0634587 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.44001e+07s, dt:234460s, Cycle: 655 +well_1Control: BHP (at the specified reference elevation): 26530125.530868836 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 5.50e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; ( R ) = ( 6.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.35e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 1.01e-14 ) ; ( R ) = ( 7.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0507434 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645137 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.46345e+07s, dt:247387s, Cycle: 656 +well_1Control: BHP (at the specified reference elevation): 26545526.020346083 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.67e-02 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 5.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 3.92e-14 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 6.07e-15 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0531779 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679263 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.48819e+07s, dt:118096s, Cycle: 657 +well_1Control: BHP (at the specified reference elevation): 26561683.419389598 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 5.47e-08 ) ; ( R ) = ( 2.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 3.42e-10 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.10e-05 ) ; ( Rwell ) = ( 9.02e-16 ) ; ( R ) = ( 2.10e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.026105 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0323963 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.5e+07s, dt:183988s, Cycle: 658 +well_1Control: BHP (at the specified reference elevation): 26569453.633564234 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 5.51e-08 ) ; ( R ) = ( 3.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 3.10e-09 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 8.14e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.89e-04 ) ; ( Rwell ) = ( 4.39e-14 ) ; ( R ) = ( 7.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0396794 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0511826 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.5609e+07, 1.56482e+07, 1.56871e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.1029e+06, 3.18105e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.023 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.57658, 726.446 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1701.28, 702938 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 381.044, 212222 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1320.23, 490716 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 56.2269, 0.338621 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1645.05, 702938 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1701.28, 0 }, { 779.317, 702143 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.55584e+07, 1.55934e+07, 1.56276e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.05232e+06, 3.12157e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.34 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00396244, 223.336 } rm^3 +compflowStatistics, caprock: Phase mass: { 1.47058, 216055 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 1.47058, 64817.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { -2.22045e-16, 151238 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 1.47058, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216055 } kg +compflowStatistics, caprock: Dissolved component mass: { { 1.47058, 0 }, { 36.5782, 216018 } } kg +well_1Control: BHP (at the specified reference elevation): 26581469.911639445 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 63.0199 +compflowStatistics: Max component CFL number: 85.8371 +Time: 8.5184e+07s, dt:224161s, Cycle: 659 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.47e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 4.56e-09 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.21e-09 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.26e-04 ) ; ( Rwell ) = ( 3.70e-14 ) ; ( R ) = ( 4.26e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0482329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607064 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.54081e+07s, dt:245928s, Cycle: 660 +well_1Control: BHP (at the specified reference elevation): 26596123.67644512 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 5.47e-08 ) ; ( R ) = ( 4.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-03 ) ; ( Rwell ) = ( 2.24e-12 ) ; ( R ) = ( 1.15e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.30e-04 ) ; ( Rwell ) = ( 8.80e-15 ) ; ( R ) = ( 2.30e-04 ) ; + Last LinSolve(iter,res) = ( 7, 1.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0527867 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664623 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.56541e+07s, dt:254503s, Cycle: 661 +well_1Control: BHP (at the specified reference elevation): 26612199.07397178 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 5.46e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.78e-02 ) ; ( Rwell ) = ( 5.78e-09 ) ; ( R ) = ( 7.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.39e-05 ) ; ( Rwell ) = ( 2.16e-13 ) ; ( R ) = ( 6.39e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.054379 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.59086e+07s, dt:91418.9s, Cycle: 662 +well_1Control: BHP (at the specified reference elevation): 26628770.910828676 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; ( R ) = ( 1.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 7.83e-10 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.02e-04 ) ; ( Rwell ) = ( 6.93e-14 ) ; ( R ) = ( 3.02e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0202321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0245917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.6e+07s, dt:161079s, Cycle: 663 +well_1Control: BHP (at the specified reference elevation): 26634753.567761496 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 5.46e-08 ) ; ( R ) = ( 2.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 2.29e-09 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 6.10e-10 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.71e-04 ) ; ( Rwell ) = ( 2.33e-14 ) ; ( R ) = ( 6.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26645243.428020954 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0346714 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0437202 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.56412e+07, 1.56805e+07, 1.57193e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.1359e+06, 3.21404e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.046 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.625, 726.421 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1724.26, 702932 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 383.408, 212235 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1340.85, 490697 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 57.5662, 0.338628 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1666.69, 702931 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1724.26, 0 }, { 782.719, 702133 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.55908e+07, 1.56256e+07, 1.56599e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.08543e+06, 3.15457e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.347 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00478013, 223.342 } rm^3 +compflowStatistics, caprock: Phase mass: { 1.77923, 216067 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 1.77923, 64821.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151246 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 1.77923, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216067 } kg +compflowStatistics, caprock: Dissolved component mass: { { 1.77923, 0 }, { 38.7793, 216028 } } kg +compflowStatistics: Max phase CFL number: 55.0116 +compflowStatistics: Max component CFL number: 74.9342 +Time: 8.61611e+07s, dt:214854s, Cycle: 664 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 4.06e-09 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.09e-04 ) ; ( Rwell ) = ( 1.12e-13 ) ; ( R ) = ( 3.09e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0459968 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565963 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.63759e+07s, dt:246294s, Cycle: 665 +well_1Control: BHP (at the specified reference elevation): 26659240.50978926 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 5.39e-09 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 8.11e-10 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 1.09e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 2.04e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.09e-05 ) ; ( Rwell ) = ( 3.52e-14 ) ; ( R ) = ( 7.09e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0526796 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650652 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.66222e+07s, dt:258440s, Cycle: 666 +well_1Control: BHP (at the specified reference elevation): 26675306.096388396 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 5.86e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.53e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-04 ) ; ( Rwell ) = ( 5.36e-14 ) ; ( R ) = ( 1.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0550208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681865 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.68807e+07s, dt:119333s, Cycle: 667 +well_1Control: BHP (at the specified reference elevation): 26692079.359372407 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 5.40e-08 ) ; ( R ) = ( 2.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-04 ) ; ( Rwell ) = ( 4.32e-13 ) ; ( R ) = ( 1.31e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0260016 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0319182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.7e+07s, dt:187242s, Cycle: 668 +well_1Control: BHP (at the specified reference elevation): 26699871.956089705 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 5.44e-08 ) ; ( R ) = ( 3.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.93e-08 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.75e-04 ) ; ( Rwell ) = ( 5.25e-13 ) ; ( R ) = ( 7.75e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0401066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0481176 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.5675e+07, 1.57142e+07, 1.57531e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.16882e+06, 3.24696e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.071 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.67564, 726.395 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1748.41, 702925 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 385.935, 212248 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1362.48, 490678 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 59.3725, 0.338639 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1689.04, 702925 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1748.41, 0 }, { 786.231, 702123 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.56246e+07, 1.56594e+07, 1.56936e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.11843e+06, 3.18749e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.355 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00575212, 223.349 } rm^3 +compflowStatistics, caprock: Phase mass: { 2.14755, 216080 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 2.14755, 64825.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151254 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 2.14755, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216080 } kg +compflowStatistics, caprock: Dissolved component mass: { { 2.14755, 0 }, { 41.0838, 216038 } } kg +well_1Control: BHP (at the specified reference elevation): 26712044.862447884 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 63.7514 +compflowStatistics: Max component CFL number: 86.8466 +Time: 8.71872e+07s, dt:236538s, Cycle: 669 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 5.41e-08 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 4.79e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 1.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.04e-04 ) ; ( Rwell ) = ( 3.17e-14 ) ; ( R ) = ( 3.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.92e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26727398.08021205 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0503335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604011 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.74238e+07s, dt:260337s, Cycle: 670 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 5.39e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 5.79e-09 ) ; ( R ) = ( 5.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 1.53e-13 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.07e-06 ) ; ( Rwell ) = ( 9.02e-15 ) ; ( R ) = ( 9.07e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0552154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667783 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.76841e+07s, dt:268578s, Cycle: 671 +well_1Control: BHP (at the specified reference elevation): 26744251.886500042 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.38e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 6.07e-09 ) ; ( R ) = ( 5.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.86e-14 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0567884 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697137 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.79527e+07s, dt:47304.2s, Cycle: 672 +well_1Control: BHP (at the specified reference elevation): 26761620.501082595 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.08e-03 ) ; ( Rwell ) = ( 5.37e-08 ) ; ( R ) = ( 8.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 2.11e-10 ) ; ( R ) = ( 6.72e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-04 ) ; ( Rwell ) = ( 8.43e-14 ) ; ( R ) = ( 1.51e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.012261 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 8.8e+07s, dt:94608.4s, Cycle: 673 +well_1Control: BHP (at the specified reference elevation): 26764715.08590617 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 5.43e-08 ) ; ( R ) = ( 1.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 7.83e-10 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 2.50e-14 ) ; ( R ) = ( 6.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0206388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0237619 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.57047e+07, 1.5744e+07, 1.57829e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.20161e+06, 3.27974e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.093 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.72016, 726.372 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1769.75, 702920 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 388.132, 212259 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1381.62, 490661 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 60.667, 0.338648 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1709.08, 702919 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1769.75, 0 }, { 789.331, 702115 } } kg +well_1Control: BHP (at the specified reference elevation): 26770884.952998325 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.56544e+07, 1.56892e+07, 1.57234e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.15134e+06, 3.22028e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.361 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00671175, 223.355 } rm^3 +compflowStatistics, caprock: Phase mass: { 2.51254, 216090 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 2.51254, 64829.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151261 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 2.51254, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216090 } kg +compflowStatistics, caprock: Dissolved component mass: { { 2.51254, 0 }, { 43.1092, 216047 } } kg +compflowStatistics: Max phase CFL number: 32.1253 +compflowStatistics: Max component CFL number: 43.7666 +Time: 8.80946e+07s, dt:169053s, Cycle: 674 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 5.41e-08 ) ; ( R ) = ( 2.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 6.45e-10 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.40e-03 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 1.65e-10 ) ; ( R ) = ( 6.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.77e-05 ) ; ( Rwell ) = ( 2.25e-14 ) ; ( R ) = ( 2.77e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0360527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0421489 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.82637e+07s, dt:230082s, Cycle: 675 +well_1Control: BHP (at the specified reference elevation): 26781845.083920877 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.19e-09 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-04 ) ; ( Rwell ) = ( 1.28e-13 ) ; ( R ) = ( 2.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0487419 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0579503 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.84937e+07s, dt:259909s, Cycle: 676 +well_1Control: BHP (at the specified reference elevation): 26796745.490890115 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 5.36e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; ( R ) = ( 5.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-03 ) ; ( Rwell ) = ( 3.64e-14 ) ; ( R ) = ( 1.70e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.73e-06 ) ; ( Rwell ) = ( 6.98e-16 ) ; ( R ) = ( 1.73e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0549994 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065664 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.87537e+07s, dt:246347s, Cycle: 677 +well_1Control: BHP (at the specified reference elevation): 26813575.809378237 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.36e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 5.01e-09 ) ; ( R ) = ( 8.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 2.87e-09 ) ; ( R ) = ( 5.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 3.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 4.01e-13 ) ; ( R ) = ( 5.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0518943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0617931 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.9e+07s, dt:267235s, Cycle: 678 +well_1Control: BHP (at the specified reference elevation): 26829450.770229362 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 5.33e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 5.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 5.52e-14 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.25e-06 ) ; ( Rwell ) = ( 6.04e-15 ) ; ( R ) = ( 9.25e-06 ) ; + Last LinSolve(iter,res) = ( 7, 3.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0559351 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641546 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.5743e+07, 1.57823e+07, 1.58212e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.23435e+06, 3.31248e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.12 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.77732, 726.343 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1797.29, 702913 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 390.936, 212274 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1406.35, 490639 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 62.4893, 0.338662 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1734.8, 702912 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1797.29, 0 }, { 793.334, 702103 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.56929e+07, 1.57276e+07, 1.57617e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.18416e+06, 3.25302e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.37 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00809064, 223.362 } rm^3 +compflowStatistics, caprock: Phase mass: { 3.03914, 216104 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 3.03914, 64833.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 151271 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.03914, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 216104 } kg +compflowStatistics, caprock: Dissolved component mass: { { 3.03914, 0 }, { 45.7094, 216058 } } kg +well_1Control: BHP (at the specified reference elevation): 26846608.67485772 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 90.4302 +compflowStatistics: Max component CFL number: 123.212 +Time: 8.92672e+07s, dt:282989s, Cycle: 679 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 5.30e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 6.49e-09 ) ; ( R ) = ( 5.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 9.66e-14 ) ; ( R ) = ( 4.54e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0594185 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683395 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.95502e+07s, dt:287536s, Cycle: 680 +well_1Control: BHP (at the specified reference elevation): 26864852.772670932 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 5.32e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 6.76e-09 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.33e-03 ) ; ( Rwell ) = ( 1.31e-12 ) ; ( R ) = ( 4.33e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 1.29e-14 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.04e-06 ) ; ( Rwell ) = ( 4.84e-15 ) ; ( R ) = ( 7.04e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0602329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0705447 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.98378e+07s, dt:162241s, Cycle: 681 +well_1Control: BHP (at the specified reference elevation): 26883362.238813065 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 5.31e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 2.19e-09 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 5.76e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.57e-04 ) ; ( Rwell ) = ( 2.57e-15 ) ; ( R ) = ( 1.57e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0345334 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0387997 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9e+07s, dt:230831s, Cycle: 682 +well_1Control: BHP (at the specified reference elevation): 26893866.346778437 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 5.34e-08 ) ; ( R ) = ( 3.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.99e-04 ) ; ( Rwell ) = ( 2.90e-12 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0482658 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544145 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.57744e+07, 1.58137e+07, 1.58525e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.26694e+06, 3.34506e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.143 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.82409, 726.319 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1819.94, 702907 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 393.196, 212286 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1426.74, 490621 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 64.0434, 0.338671 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1755.9, 702907 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1819.94, 0 }, { 796.577, 702094 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.57244e+07, 1.5759e+07, 1.57931e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.21684e+06, 3.28561e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.377 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.00934042, 223.368 } rm^3 +compflowStatistics, caprock: Phase mass: { 3.51844, 216115 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 3.51824, 64837.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.000202391, 151278 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.51321, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.00523289, 216115 } kg +compflowStatistics, caprock: Dissolved component mass: { { 3.51844, 0 }, { 47.8296, 216067 } } kg +well_1Control: BHP (at the specified reference elevation): 26908665.506661154 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 77.8918 +compflowStatistics: Max component CFL number: 106.137 +Time: 9.02308e+07s, dt:271066s, Cycle: 683 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 1.52e-09 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.07e-14 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.16e-06 ) ; ( Rwell ) = ( 1.32e-15 ) ; ( R ) = ( 9.16e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0563168 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639691 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.05019e+07s, dt:287584s, Cycle: 684 +well_1Control: BHP (at the specified reference elevation): 26925997.302441068 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 5.26e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 6.52e-09 ) ; ( R ) = ( 5.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.72e-09 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 2.49e-13 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.95e-06 ) ; ( Rwell ) = ( 2.78e-15 ) ; ( R ) = ( 8.95e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0601227 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692017 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.07895e+07s, dt:210519s, Cycle: 685 +well_1Control: BHP (at the specified reference elevation): 26944498.539700232 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; ( R ) = ( 3.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.58e-09 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 9.23e-10 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.15e-04 ) ; ( Rwell ) = ( 9.61e-14 ) ; ( R ) = ( 2.15e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0443057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0494992 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.1e+07s, dt:261594s, Cycle: 686 +well_1Control: BHP (at the specified reference elevation): 26958064.311500385 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 5.29e-08 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 5.31e-09 ) ; ( R ) = ( 4.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.59e-04 ) ; ( Rwell ) = ( 3.41e-14 ) ; ( R ) = ( 4.59e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0544954 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600852 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 26974833.89529444 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.58079e+07, 1.58472e+07, 1.5886e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.29942e+06, 3.37755e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.168 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.87387, 726.294 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1844.17, 702901 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 395.665, 212299 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1448.5, 490603 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 65.707, 0.338681 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1778.46, 702901 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1844.17, 0 }, { 800.014, 702085 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.57579e+07, 1.57925e+07, 1.58266e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.24943e+06, 3.31809e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.384 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0107917, 223.374 } rm^3 +compflowStatistics, caprock: Phase mass: { 4.07725, 216127 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 4.07588, 64841.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.0013759, 151286 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.04526, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.0319988, 216127 } kg +compflowStatistics, caprock: Dissolved component mass: { { 4.07725, 0 }, { 50.082, 216076 } } kg +compflowStatistics: Max phase CFL number: 88.0086 +compflowStatistics: Max component CFL number: 119.931 +Time: 9.12616e+07s, dt:288871s, Cycle: 687 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 5.26e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 6.48e-09 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 5.84e-14 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.90e-04 ) ; ( Rwell ) = ( 5.06e-15 ) ; ( R ) = ( 1.90e-04 ) ; + Last LinSolve(iter,res) = ( 8, 2.04e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 26993294.36453728 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0598708 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660282 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.15505e+07s, dt:300227s, Cycle: 688 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 5.24e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 4.91e-08 ) ; ( R ) = ( 5.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 2.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.82e-09 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 4.88e-14 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.16e-05 ) ; ( Rwell ) = ( 2.90e-15 ) ; ( R ) = ( 3.16e-05 ) ; + Last LinSolve(iter,res) = ( 9, 1.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0623322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701757 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.18507e+07s, dt:149308s, Cycle: 689 +well_1Control: BHP (at the specified reference elevation): 27012534.883652397 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 5.25e-08 ) ; ( R ) = ( 2.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.76e-09 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 2.27e-14 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.93e-04 ) ; ( Rwell ) = ( 2.42e-15 ) ; ( R ) = ( 3.93e-04 ) ; + Last LinSolve(iter,res) = ( 6, 1.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0315723 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0344506 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.2e+07s, dt:225734s, Cycle: 690 +well_1Control: BHP (at the specified reference elevation): 27022151.99806243 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 5.28e-08 ) ; ( R ) = ( 3.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 3.87e-09 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-04 ) ; ( Rwell ) = ( 7.38e-14 ) ; ( R ) = ( 2.01e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0468338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.050825 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.58392e+07, 1.58784e+07, 1.59173e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.33186e+06, 3.40998e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.19 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.92025, 726.27 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1866.84, 702896 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 397.899, 212310 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1468.94, 490585 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 67.3686, 0.33869 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1799.47, 702895 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1866.84, 0 }, { 803.189, 702076 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.57893e+07, 1.58238e+07, 1.58578e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.28193e+06, 3.35053e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.391 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0122576, 223.379 } rm^3 +compflowStatistics, caprock: Phase mass: { 4.64395, 216138 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 4.63959, 64845 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.00436218, 151293 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.55747, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.0864822, 216138 } kg +compflowStatistics, caprock: Dissolved component mass: { { 4.64395, 0 }, { 52.1718, 216085 } } kg +well_1Control: BHP (at the specified reference elevation): 27036556.93075853 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 75.7332 +compflowStatistics: Max component CFL number: 103.211 +Time: 9.22257e+07s, dt:276168s, Cycle: 691 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 5.70e-09 ) ; ( R ) = ( 5.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.75e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.51e-09 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.60e-04 ) ; ( Rwell ) = ( 9.97e-14 ) ; ( R ) = ( 3.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0570756 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061714 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.25019e+07s, dt:299829s, Cycle: 692 +well_1Control: BHP (at the specified reference elevation): 27054155.903471947 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 5.21e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 6.77e-09 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.75e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.29e-04 ) ; ( Rwell ) = ( 1.11e-13 ) ; ( R ) = ( 7.29e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0617495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683528 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.28017e+07s, dt:198270s, Cycle: 693 +well_1Control: BHP (at the specified reference elevation): 27073226.373225972 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; ( R ) = ( 2.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 2.97e-09 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 1.06e-12 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-04 ) ; ( Rwell ) = ( 1.09e-14 ) ; ( R ) = ( 3.22e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27085913.560581975 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0413014 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0453028 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.3e+07s, dt:259248s, Cycle: 694 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.23e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 9.31e-09 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-03 ) ; ( Rwell ) = ( 1.00e-12 ) ; ( R ) = ( 3.20e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.75e-06 ) ; ( Rwell ) = ( 7.10e-15 ) ; ( R ) = ( 6.75e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0534354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0569675 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.58725e+07, 1.59118e+07, 1.59506e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.36415e+06, 3.44226e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.214 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 4.9696, 726.245 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1891.09, 702890 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 400.324, 212323 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1490.77, 490567 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 69.0632, 0.338699 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1822.03, 702889 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1891.09, 0 }, { 806.623, 702067 } } kg +well_1Control: BHP (at the specified reference elevation): 27102419.05783748 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.58227e+07, 1.58572e+07, 1.58912e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.31435e+06, 3.38282e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.399 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0139448, 223.385 } rm^3 +compflowStatistics, caprock: Phase mass: { 5.29873, 216150 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 5.28726, 64849 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.0114718, 151301 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.11714, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.181592, 216150 } kg +compflowStatistics, caprock: Dissolved component mass: { { 5.29873, 0 }, { 54.3907, 216094 } } kg +compflowStatistics: Max phase CFL number: 86.7198 +compflowStatistics: Max component CFL number: 118.192 +Time: 9.32592e+07s, dt:295985s, Cycle: 695 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 5.20e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.12e-04 ) ; ( Rwell ) = ( 1.94e-13 ) ; ( R ) = ( 7.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.06086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643308 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.35552e+07s, dt:312878s, Cycle: 696 +well_1Control: BHP (at the specified reference elevation): 27121244.01799635 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 7.13e-09 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.87e-09 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 7.22e-15 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 2.14e-15 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0641538 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0693244 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.38681e+07s, dt:131889s, Cycle: 697 +well_1Control: BHP (at the specified reference elevation): 27141114.408008233 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; ( R ) = ( 1.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.32e-09 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-04 ) ; ( Rwell ) = ( 6.69e-14 ) ; ( R ) = ( 2.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0277851 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0296156 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.4e+07s, dt:214318s, Cycle: 698 +well_1Control: BHP (at the specified reference elevation): 27149573.28984922 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 3.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.53e-02 ) ; ( Rwell ) = ( 3.36e-09 ) ; ( R ) = ( 9.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 1.92e-09 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.53e-04 ) ; ( Rwell ) = ( 4.20e-13 ) ; ( R ) = ( 6.53e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0442662 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0461794 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.59033e+07, 1.59426e+07, 1.59814e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.39639e+06, 3.4745e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.237 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.01515, 726.222 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1913.58, 702885 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 402.549, 212335 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1511.03, 490549 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 70.6598, 0.33871 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1842.92, 702884 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1913.58, 0 }, { 809.694, 702058 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.58536e+07, 1.5888e+07, 1.5922e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.34666e+06, 3.41506e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.405 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0156098, 223.39 } rm^3 +compflowStatistics, caprock: Phase mass: { 5.94754, 216160 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 5.92438, 64852.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.023158, 151307 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.62907, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.318464, 216160 } kg +compflowStatistics, caprock: Dissolved component mass: { { 5.94754, 0 }, { 56.4241, 216103 } } kg +well_1Control: BHP (at the specified reference elevation): 27163226.686722703 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 71.4956 +compflowStatistics: Max component CFL number: 97.4504 +Time: 9.42143e+07s, dt:277206s, Cycle: 699 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; ( R ) = ( 3.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 5.53e-09 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 3.71e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.01e-05 ) ; ( Rwell ) = ( 7.77e-15 ) ; ( R ) = ( 7.01e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0567215 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0596518 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.44915e+07s, dt:307513s, Cycle: 700 +well_1Control: BHP (at the specified reference elevation): 27180788.201455697 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 6.71e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 3.06e-09 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.69e-04 ) ; ( Rwell ) = ( 7.81e-14 ) ; ( R ) = ( 7.69e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0628258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654219 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.4799e+07s, dt:200963s, Cycle: 701 +well_1Control: BHP (at the specified reference elevation): 27200277.366678473 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; ( R ) = ( 2.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.93e-09 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 7.61e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 1.63e-13 ) ; ( R ) = ( 4.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0415548 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0438878 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.5e+07s, dt:267482s, Cycle: 702 +well_1Control: BHP (at the specified reference elevation): 27213090.876478143 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 5.17e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 5.09e-09 ) ; ( R ) = ( 5.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.31e-09 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 1.15e-14 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 1.34e-15 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0546562 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575095 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.59372e+07, 1.59764e+07, 1.60153e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.42857e+06, 3.50668e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.261 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.06511, 726.196 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1938.35, 702879 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 404.97, 212348 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1533.38, 490531 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 72.3519, 0.338722 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1866, 702878 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1938.35, 0 }, { 813.072, 702049 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.58875e+07, 1.59219e+07, 1.59558e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.37891e+06, 3.44724e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.413 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0175628, 223.395 } rm^3 +compflowStatistics, caprock: Phase mass: { 6.71154, 216172 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 6.66807, 64856.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.0434761, 151315 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.1998, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.511737, 216172 } kg +compflowStatistics, caprock: Dissolved component mass: { { 6.71154, 0 }, { 58.6454, 216112 } } kg +well_1Control: BHP (at the specified reference elevation): 27230041.47994388 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 88.9649 +compflowStatistics: Max component CFL number: 121.272 +Time: 9.52675e+07s, dt:303597s, Cycle: 703 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 6.40e-09 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 4.57e-15 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.42e-06 ) ; ( Rwell ) = ( 6.01e-16 ) ; ( R ) = ( 4.42e-06 ) ; + Last LinSolve(iter,res) = ( 9, 1.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0616907 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627647 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.55711e+07s, dt:326065s, Cycle: 704 +well_1Control: BHP (at the specified reference elevation): 27249200.370333895 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 5.11e-08 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-02 ) ; ( Rwell ) = ( 7.31e-09 ) ; ( R ) = ( 5.50e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.22e-04 ) ; ( Rwell ) = ( 1.27e-13 ) ; ( R ) = ( 6.22e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0661244 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0673023 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.58971e+07s, dt:102856s, Cycle: 705 +well_1Control: BHP (at the specified reference elevation): 27269764.476457 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; ( R ) = ( 1.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.61e-03 ) ; ( Rwell ) = ( 7.71e-10 ) ; ( R ) = ( 9.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-04 ) ; ( Rwell ) = ( 1.25e-14 ) ; ( R ) = ( 4.04e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0215768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0214856 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.6e+07s, dt:191196s, Cycle: 706 +well_1Control: BHP (at the specified reference elevation): 27276307.656251077 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 5.15e-08 ) ; ( R ) = ( 2.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 2.56e-09 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.85e-03 ) ; ( Rwell ) = ( 6.61e-10 ) ; ( R ) = ( 6.85e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.75e-04 ) ; ( Rwell ) = ( 3.39e-14 ) ; ( R ) = ( 1.75e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0390987 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0406979 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.59667e+07, 1.6006e+07, 1.60448e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.46062e+06, 3.53872e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.283 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.10864, 726.174 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1960.04, 702874 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 406.999, 212359 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1553.04, 490515 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 73.8028, 0.338732 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1886.24, 702874 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1960.04, 0 }, { 816.055, 702041 } } kg +well_1Control: BHP (at the specified reference elevation): 27288391.889252037 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.59172e+07, 1.59515e+07, 1.59854e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.41106e+06, 3.47929e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.42 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0193739, 223.4 } rm^3 +compflowStatistics, caprock: Phase mass: { 7.42283, 216181 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 7.35317, 64860.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.0696668, 151321 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.69556, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0.727274, 216181 } kg +compflowStatistics, caprock: Dissolved component mass: { { 7.42283, 0 }, { 60.5748, 216120 } } kg +compflowStatistics: Max phase CFL number: 63.427 +compflowStatistics: Max component CFL number: 86.4662 +Time: 9.61912e+07s, dt:265207s, Cycle: 707 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 5.11e-08 ) ; ( R ) = ( 3.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.68e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.01e-04 ) ; ( Rwell ) = ( 3.39e-12 ) ; ( R ) = ( 4.01e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0534966 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0552174 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.64564e+07s, dt:308663s, Cycle: 708 +well_1Control: BHP (at the specified reference elevation): 27305015.787497815 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 6.35e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 4.34e-10 ) ; ( R ) = ( 7.68e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.95e-04 ) ; ( Rwell ) = ( 4.23e-14 ) ; ( R ) = ( 2.95e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.32e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27324383.383070946 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0622376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0634773 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.67651e+07s, dt:234934s, Cycle: 709 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 5.06e-08 ) ; ( R ) = ( 3.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 3.74e-09 ) ; ( R ) = ( 5.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 9.88e-10 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 2.48e-13 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0479257 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0477733 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.7e+07s, dt:298020s, Cycle: 710 +well_1Control: BHP (at the specified reference elevation): 27339234.625210434 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 5.95e-09 ) ; ( R ) = ( 8.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 2.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 1.16e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 2.92e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.56e-02 ) ; ( Rwell ) = ( 3.01e-09 ) ; ( R ) = ( 9.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 3.17e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 4.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 2.35e-09 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 2.99e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 3.92e-14 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.97e-05 ) ; ( Rwell ) = ( 1.54e-17 ) ; ( R ) = ( 8.97e-05 ) ; + Last LinSolve(iter,res) = ( 7, 3.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.060411 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618736 +compflowStatistics, reservoir: Pressure (min, average, max): 1.60021e+07, 1.60413e+07, 1.60802e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.49252e+06, 3.57062e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.309 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.16047, 726.148 } rm^3 +compflowStatistics, reservoir: Phase mass: { 1985.99, 702868 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 409.603, 212373 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1576.39, 490495 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 75.7695, 0.338744 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1910.22, 702868 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 1985.99, 0 }, { 819.635, 702032 } } kg +well_1Control: BHP (at the specified reference elevation): 27358039.22620385 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.59526e+07, 1.59868e+07, 1.60207e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.44309e+06, 3.51119e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.427 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0216624, 223.406 } rm^3 +compflowStatistics, caprock: Phase mass: { 8.32521, 216193 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 8.21317, 64864.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.112042, 151329 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.31264, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 1.01257, 216193 } kg +compflowStatistics, caprock: Dissolved component mass: { { 8.32521, 0 }, { 62.8655, 216129 } } kg +compflowStatistics: Max phase CFL number: 98.5595 +compflowStatistics: Max component CFL number: 134.371 +Time: 9.7298e+07s, dt:298020s, Cycle: 711 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 5.08e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 5.93e-09 ) ; ( R ) = ( 2.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 4.57e-09 ) ; ( R ) = ( 1.58e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.17e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 4.01e-09 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 3.54e-09 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.78e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 3.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.23e-02 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 8.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 3.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.18e-02 ) ; ( Rwell ) = ( 2.74e-09 ) ; ( R ) = ( 8.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.55e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 3.02e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 3.58e-13 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.37e-05 ) ; ( Rwell ) = ( 5.27e-15 ) ; ( R ) = ( 1.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0599144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604933 +Time: 9.7596e+07s, dt:298020s, Cycle: 712 +well_1Control: BHP (at the specified reference elevation): 27376713.37226847 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 5.04e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 5.81e-09 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.93e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.49e-04 ) ; ( Rwell ) = ( 1.48e-15 ) ; ( R ) = ( 6.49e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0600359 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593662 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.78941e+07s, dt:105939s, Cycle: 713 +well_1Control: BHP (at the specified reference elevation): 27395421.765206 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 1.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 1.17e-12 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.10e-06 ) ; ( Rwell ) = ( 2.59e-15 ) ; ( R ) = ( 4.10e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0220022 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0209877 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.8e+07s, dt:198680s, Cycle: 714 +well_1Control: BHP (at the specified reference elevation): 27402124.8873479 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 5.09e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 2.60e-09 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 6.93e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.33e-05 ) ; ( Rwell ) = ( 8.15e-14 ) ; ( R ) = ( 7.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0404423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0395761 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.60308e+07, 1.607e+07, 1.61089e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.52442e+06, 3.60252e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.33 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.20261, 726.127 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2007.18, 702864 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 411.62, 212384 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1595.56, 490480 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 77.1967, 0.338753 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1929.99, 702863 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2007.18, 0 }, { 822.453, 702024 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.59814e+07, 1.60155e+07, 1.60495e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.47504e+06, 3.54309e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.434 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0236199, 223.41 } rm^3 +compflowStatistics, caprock: Phase mass: { 9.10022, 216203 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 8.94444, 64867.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.15578, 151335 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.82072, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 1.2795, 216203 } kg +compflowStatistics, caprock: Dissolved component mass: { { 9.10022, 0 }, { 64.7133, 216137 } } kg +well_1Control: BHP (at the specified reference elevation): 27414672.391533196 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 65.5417 +compflowStatistics: Max component CFL number: 89.3625 +Time: 9.81987e+07s, dt:279733s, Cycle: 715 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 5.07e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 5.14e-09 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.67e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 1.12e-13 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.056492 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0570781 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.84784e+07s, dt:318989s, Cycle: 716 +well_1Control: BHP (at the specified reference elevation): 27432284.71808157 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 5.05e-08 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 6.55e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 1.70e-09 ) ; ( R ) = ( 3.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.48e-03 ) ; ( Rwell ) = ( 4.39e-10 ) ; ( R ) = ( 6.48e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.58e-04 ) ; ( Rwell ) = ( 2.06e-14 ) ; ( R ) = ( 3.58e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.60e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27452233.433542155 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0638571 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640001 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.87974e+07s, dt:202598s, Cycle: 717 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 5.01e-08 ) ; ( R ) = ( 2.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.65e-09 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.47e-04 ) ; ( Rwell ) = ( 3.37e-13 ) ; ( R ) = ( 9.47e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0406754 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0400436 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.9e+07s, dt:283473s, Cycle: 718 +well_1Control: BHP (at the specified reference elevation): 27464869.94483408 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 3.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.85e-02 ) ; ( Rwell ) = ( 5.03e-09 ) ; ( R ) = ( 3.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.11e-04 ) ; ( Rwell ) = ( 1.04e-13 ) ; ( R ) = ( 5.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0565228 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0552657 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.60652e+07, 1.61045e+07, 1.61433e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.55626e+06, 3.63435e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.355 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.25297, 726.102 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2032.62, 702858 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 413.973, 212397 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1618.65, 490461 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 79.0279, 0.406346 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1953.6, 702858 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2032.62, 0 }, { 825.899, 702016 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.6016e+07, 1.605e+07, 1.60839e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.50696e+06, 3.57493e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.441 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0260869, 223.415 } rm^3 +compflowStatistics, caprock: Phase mass: { 10.0807, 216214 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 9.86003, 64871.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.220632, 151342 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.44754, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 1.63313, 216214 } kg +compflowStatistics, caprock: Dissolved component mass: { { 10.0807, 0 }, { 66.9211, 216146 } } kg +well_1Control: BHP (at the specified reference elevation): 27482513.385918163 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 93.2344 +compflowStatistics: Max component CFL number: 127.13 +Time: 9.92835e+07s, dt:329745s, Cycle: 719 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 2.66e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 2.90e-08 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.47e-04 ) ; ( Rwell ) = ( 4.16e-12 ) ; ( R ) = ( 6.47e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0658011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064035 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.96132e+07s, dt:349606s, Cycle: 720 +well_1Control: BHP (at the specified reference elevation): 27503109.551898174 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 7.65e-09 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 1.97e-09 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.15e-04 ) ; ( Rwell ) = ( 9.09e-14 ) ; ( R ) = ( 5.15e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0694349 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690027 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.99628e+07s, dt:37176s, Cycle: 721 +well_1Control: BHP (at the specified reference elevation): 27524860.424469694 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-03 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 9.77e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.77e-05 ) ; ( Rwell ) = ( 5.12e-14 ) ; ( R ) = ( 5.77e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00812605 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00728371 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1e+08s, dt:74352s, Cycle: 722 +well_1Control: BHP (at the specified reference elevation): 27527192.785793193 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.52e-03 ) ; ( Rwell ) = ( 5.01e-08 ) ; ( R ) = ( 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.54e-03 ) ; ( Rwell ) = ( 3.59e-10 ) ; ( R ) = ( 8.54e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 4.62e-13 ) ; ( R ) = ( 7.99e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.29e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27531845.533564743 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0153878 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.01435 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.60903e+07, 1.61295e+07, 1.61683e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.58789e+06, 3.66598e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.373 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.28952, 726.083 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2051.17, 702854 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 415.716, 212407 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1635.45, 490448 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 80.0847, 0.406356 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1971.08, 702854 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2051.17, 0 }, { 828.395, 702009 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.60411e+07, 1.60751e+07, 1.61089e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.53873e+06, 3.60656e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.447 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0279591, 223.419 } rm^3 +compflowStatistics, caprock: Phase mass: { 10.8275, 216222 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 10.5496, 64874.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.277956, 151347 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.89069, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 1.93683, 216222 } kg +compflowStatistics, caprock: Dissolved component mass: { { 10.8275, 0 }, { 68.5177, 216152 } } kg +compflowStatistics: Max phase CFL number: 24.4014 +compflowStatistics: Max component CFL number: 33.2747 +Time: 1.00074e+08s, dt:148704s, Cycle: 723 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 1.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.38e-09 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.81e-03 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 3.59e-10 ) ; ( R ) = ( 8.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-04 ) ; ( Rwell ) = ( 1.69e-13 ) ; ( R ) = ( 1.89e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.029947 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0284905 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00223e+08s, dt:245925s, Cycle: 724 +well_1Control: BHP (at the specified reference elevation): 27541109.87170292 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 3.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 3.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 9.78e-10 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 2.50e-10 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 6.63e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 9.87e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.76e-03 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 6.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.60e-05 ) ; ( Rwell ) = ( 2.70e-14 ) ; ( R ) = ( 9.60e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.82e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27556407.99574054 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0489977 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0469949 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00469e+08s, dt:314924s, Cycle: 725 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 6.03e-09 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 4.11e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 5.11e-15 ) ; ( R ) = ( 3.39e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0625978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600358 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00784e+08s, dt:216095s, Cycle: 726 +well_1Control: BHP (at the specified reference elevation): 27576021.011437148 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 4.96e-08 ) ; ( R ) = ( 2.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 7.66e-10 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.30e-04 ) ; ( Rwell ) = ( 1.66e-13 ) ; ( R ) = ( 3.30e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0434745 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0421732 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01e+08s, dt:294013s, Cycle: 727 +well_1Control: BHP (at the specified reference elevation): 27589571.135657206 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.99e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 5.38e-08 ) ; ( R ) = ( 3.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e-03 ) ; ( Rwell ) = ( 1.08e-12 ) ; ( R ) = ( 3.01e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 6.35e-15 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 7, 3.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-06 ) ; ( Rwell ) = ( 4.29e-15 ) ; ( R ) = ( 1.75e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0583255 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0563753 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.61289e+07, 1.61681e+07, 1.62069e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.61956e+06, 3.69765e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.401 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.34584, 726.055 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2079.86, 702848 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 418.501, 212421 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1661.36, 490427 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 82.2849, 0.406372 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 1997.57, 702848 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2079.86, 0 }, { 832.116, 701999 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.60797e+07, 1.61137e+07, 1.61475e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.57041e+06, 3.63823e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.456 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0309709, 223.425 } rm^3 +compflowStatistics, caprock: Phase mass: { 12.0338, 216234 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 11.6466, 64879.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.387179, 151355 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.47827, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 2.55549, 216234 } kg +compflowStatistics, caprock: Dissolved component mass: { { 12.0338, 0 }, { 70.9602, 216162 } } kg +well_1Control: BHP (at the specified reference elevation): 27607856.52045875 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 96.1704 +compflowStatistics: Max component CFL number: 131.154 +Time: 1.01294e+08s, dt:337853s, Cycle: 728 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 4.95e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 6.80e-09 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.73e-09 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 3.23e-13 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.02e-05 ) ; ( Rwell ) = ( 9.76e-15 ) ; ( R ) = ( 2.02e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0664204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631049 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01632e+08s, dt:361598s, Cycle: 729 +well_1Control: BHP (at the specified reference elevation): 27628691.401396155 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 4.90e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 7.59e-09 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.05e-09 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.46e-13 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.02e-06 ) ; ( Rwell ) = ( 2.30e-15 ) ; ( R ) = ( 2.02e-06 ) ; + Last LinSolve(iter,res) = ( 10, 1.58e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 27651088.683639005 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0712738 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661323 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01993e+08s, dt:6535.16s, Cycle: 730 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.67e-04 ) ; ( Rwell ) = ( 4.92e-08 ) ; ( R ) = ( 7.67e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.89e-04 ) ; ( Rwell ) = ( 2.06e-11 ) ; ( R ) = ( 3.89e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00200155 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00120012 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.02e+08s, dt:13070.3s, Cycle: 731 +well_1Control: BHP (at the specified reference elevation): 27651498.533727266 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 1.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.02e-04 ) ; ( Rwell ) = ( 1.52e-11 ) ; ( R ) = ( 8.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00362715 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00240643 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.61514e+07, 1.61907e+07, 1.62295e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.65102e+06, 3.72911e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.417 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.37865, 726.039 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2096.66, 702845 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 420.135, 212430 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1676.52, 490415 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 83.6453, 0.406382 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2013.01, 702845 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2096.66, 0 }, { 834.412, 701994 } } kg +well_1Control: BHP (at the specified reference elevation): 27652318.61049462 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.61024e+07, 1.61363e+07, 1.61701e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.60202e+06, 3.66969e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.461 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0328129, 223.428 } rm^3 +compflowStatistics, caprock: Phase mass: { 12.7742, 216241 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 12.3083, 64881.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.465927, 151359 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.79557, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 2.97862, 216241 } kg +compflowStatistics, caprock: Dissolved component mass: { { 12.7742, 0 }, { 72.3871, 216167 } } kg +compflowStatistics: Max phase CFL number: 4.26694 +compflowStatistics: Max component CFL number: 5.81941 +Time: 1.02013e+08s, dt:26140.6s, Cycle: 732 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 3.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 4.37e-11 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-05 ) ; ( Rwell ) = ( 1.21e-14 ) ; ( R ) = ( 1.03e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00604284 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00482723 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.02039e+08s, dt:52281.2s, Cycle: 733 +well_1Control: BHP (at the specified reference elevation): 27653968.158258833 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-03 ) ; ( Rwell ) = ( 5.01e-08 ) ; ( R ) = ( 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.50e-03 ) ; ( Rwell ) = ( 1.68e-10 ) ; ( R ) = ( 5.50e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.32e-04 ) ; ( Rwell ) = ( 2.70e-14 ) ; ( R ) = ( 3.32e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0109931 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00969344 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.02091e+08s, dt:104562s, Cycle: 734 +well_1Control: BHP (at the specified reference elevation): 27657261.789700113 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 6.71e-10 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 7.49e-14 ) ; ( R ) = ( 8.57e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0213376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0195065 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02196e+08s, dt:201427s, Cycle: 735 +well_1Control: BHP (at the specified reference elevation): 27663820.20069859 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 4.98e-08 ) ; ( R ) = ( 2.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.44e-09 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.22e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 3.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 3.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.07e-09 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.26e-04 ) ; ( Rwell ) = ( 1.21e-13 ) ; ( R ) = ( 6.26e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0400967 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0386804 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02397e+08s, dt:287048s, Cycle: 736 +well_1Control: BHP (at the specified reference elevation): 27676355.00517594 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.93e-08 ) ; ( R ) = ( 3.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 9.15e-09 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.26e-02 ) ; ( Rwell ) = ( 6.05e-09 ) ; ( R ) = ( 5.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 5.80e-09 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 5.44e-09 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 8.66e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.08e-03 ) ; ( Rwell ) = ( 5.36e-09 ) ; ( R ) = ( 9.08e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.18e-03 ) ; ( Rwell ) = ( 1.46e-12 ) ; ( R ) = ( 1.18e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.07e-06 ) ; ( Rwell ) = ( 1.46e-15 ) ; ( R ) = ( 8.07e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0563406 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0537768 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02685e+08s, dt:315471s, Cycle: 737 +well_1Control: BHP (at the specified reference elevation): 27694050.237599637 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 5.64e-09 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.49e-09 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-03 ) ; ( Rwell ) = ( 2.03e-13 ) ; ( R ) = ( 1.16e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.77e-05 ) ; ( Rwell ) = ( 1.16e-14 ) ; ( R ) = ( 5.77e-05 ) ; + Last LinSolve(iter,res) = ( 8, 2.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0616309 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585465 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03e+08s, dt:354096s, Cycle: 738 +well_1Control: BHP (at the specified reference elevation): 27713412.571571108 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 6.94e-09 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.94e-04 ) ; ( Rwell ) = ( 2.19e-13 ) ; ( R ) = ( 9.94e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.069109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643582 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.61935e+07, 1.62328e+07, 1.62716e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.68249e+06, 3.76057e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.448 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.43975, 726.008 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2128.07, 702839 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 422.987, 212446 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1705.08, 490393 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 85.696, 0.406399 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2042.37, 702838 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2128.07, 0 }, { 838.569, 701983 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.61447e+07, 1.61785e+07, 1.62122e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.63358e+06, 3.70116e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.47 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0363831, 223.434 } rm^3 +compflowStatistics, caprock: Phase mass: { 14.2151, 216254 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 13.57, 64886.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.645092, 151367 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.322, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 3.89308, 216254 } kg +compflowStatistics, caprock: Dissolved component mass: { { 14.2151, 0 }, { 75.0254, 216178 } } kg +well_1Control: BHP (at the specified reference elevation): 27735167.341381 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 115.182 +compflowStatistics: Max component CFL number: 157.104 +Time: 1.03354e+08s, dt:374202s, Cycle: 739 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 4.86e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 5.25e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 2.06e-09 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.55e-04 ) ; ( Rwell ) = ( 6.96e-14 ) ; ( R ) = ( 5.55e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0731621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069438 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03728e+08s, dt:271702s, Cycle: 740 +well_1Control: BHP (at the specified reference elevation): 27758225.472999625 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 4.87e-08 ) ; ( R ) = ( 3.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.22e-09 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 1.10e-09 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 9.68e-10 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 8.52e-10 ) ; ( R ) = ( 3.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.60e-03 ) ; ( Rwell ) = ( 1.14e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 2.18e-10 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 5.74e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 8.54e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.21e-03 ) ; ( Rwell ) = ( 9.96e-09 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.41e-03 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.44e-03 ) ; ( Rwell ) = ( 1.91e-10 ) ; ( R ) = ( 4.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.44e-04 ) ; ( Rwell ) = ( 2.92e-14 ) ; ( R ) = ( 1.44e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0535017 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0486978 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.04e+08s, dt:340854s, Cycle: 741 +well_1Control: BHP (at the specified reference elevation): 27775040.416231543 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 4.88e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 1.87e-13 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.27e-14 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0663473 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602475 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.62245e+07, 1.62637e+07, 1.63025e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.71382e+06, 3.7919e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.47 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.48454, 725.986 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2151.21, 702834 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 425.152, 212458 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1726.06, 490376 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 87.2287, 0.406412 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2063.98, 702834 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2151.21, 0 }, { 841.571, 701976 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.61757e+07, 1.62094e+07, 1.62431e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.66497e+06, 3.73249e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.477 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0391182, 223.438 } rm^3 +compflowStatistics, caprock: Phase mass: { 15.324, 216264 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 14.5172, 64890.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.806794, 151373 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.6184, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 4.70556, 216264 } kg +compflowStatistics, caprock: Dissolved component mass: { { 15.324, 0 }, { 76.9513, 216185 } } kg +well_1Control: BHP (at the specified reference elevation): 27795970.37047975 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 110.582 +compflowStatistics: Max component CFL number: 150.841 +Time: 1.04341e+08s, dt:375754s, Cycle: 742 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 7.72e-09 ) ; ( R ) = ( 4.96e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-03 ) ; ( Rwell ) = ( 2.17e-13 ) ; ( R ) = ( 2.29e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-04 ) ; ( Rwell ) = ( 4.41e-15 ) ; ( R ) = ( 1.36e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.65e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0728046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656785 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.04717e+08s, dt:283392s, Cycle: 743 +well_1Control: BHP (at the specified reference elevation): 27818963.085531883 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; ( R ) = ( 3.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.19e-02 ) ; ( Rwell ) = ( 4.43e-09 ) ; ( R ) = ( 9.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 2.51e-09 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 6.56e-10 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-03 ) ; ( Rwell ) = ( 5.94e-14 ) ; ( R ) = ( 1.43e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-05 ) ; ( Rwell ) = ( 4.55e-15 ) ; ( R ) = ( 1.29e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0553719 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0507683 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.05e+08s, dt:346936s, Cycle: 744 +well_1Control: BHP (at the specified reference elevation): 27836399.190015882 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; ( R ) = ( 3.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 6.53e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 2.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.71e-09 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.92e-04 ) ; ( Rwell ) = ( 1.79e-13 ) ; ( R ) = ( 8.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0674577 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0608755 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.62559e+07, 1.62951e+07, 1.63339e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.74503e+06, 3.82311e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.493 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.52992, 725.963 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2174.76, 702830 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 427.351, 212470 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1747.41, 490360 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 88.8557, 0.406424 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2085.9, 702830 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2174.76, 0 }, { 844.647, 701968 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.62071e+07, 1.62409e+07, 1.62745e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.69629e+06, 3.7637e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.484 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.041998, 223.442 } rm^3 +compflowStatistics, caprock: Phase mass: { 16.4959, 216273 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 15.497, 64894.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0.998865, 151379 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.944, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 5.55189, 216273 } kg +compflowStatistics, caprock: Dissolved component mass: { { 16.4959, 0 }, { 78.8995, 216193 } } kg +well_1Control: BHP (at the specified reference elevation): 27857702.12275234 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 112.255 +compflowStatistics: Max component CFL number: 153.134 +Time: 1.05347e+08s, dt:379955s, Cycle: 745 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.82e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 7.80e-09 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.03e-09 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 2.97e-13 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 6.59e-15 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0734427 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659222 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.05727e+08s, dt:273109s, Cycle: 746 +well_1Control: BHP (at the specified reference elevation): 27880943.83289875 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; ( R ) = ( 3.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 3.05e-08 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.91e-08 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.30e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 2.89e-08 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 2.54e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 3.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.87e-08 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 2.60e-12 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.80e-05 ) ; ( Rwell ) = ( 1.60e-15 ) ; ( R ) = ( 8.80e-05 ) ; + Last LinSolve(iter,res) = ( 8, 1.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0530047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0469658 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.06e+08s, dt:349859s, Cycle: 747 +well_1Control: BHP (at the specified reference elevation): 27897656.378842987 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; ( R ) = ( 3.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 6.51e-09 ) ; ( R ) = ( 4.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.69e-09 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 1.71e-13 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e-05 ) ; ( Rwell ) = ( 2.46e-15 ) ; ( R ) = ( 1.26e-05 ) ; + Last LinSolve(iter,res) = ( 8, 3.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0677436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612294 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.62871e+07, 1.63264e+07, 1.63652e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.7762e+06, 3.85428e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.516 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.57499, 725.941 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2198.25, 702826 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 429.561, 212482 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1768.68, 490344 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 90.4845, 0.406437 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2107.76, 702825 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2198.25, 0 }, { 847.677, 701961 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.62384e+07, 1.62721e+07, 1.63058e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.72753e+06, 3.79487e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.491 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0449611, 223.446 } rm^3 +compflowStatistics, caprock: Phase mass: { 17.7064, 216283 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 16.4866, 64898 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 1.21985, 151385 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.2445, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 6.46189, 216283 } kg +compflowStatistics, caprock: Dissolved component mass: { { 17.7064, 0 }, { 80.8267, 216200 } } kg +well_1Control: BHP (at the specified reference elevation): 27919081.155828178 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 112.901 +compflowStatistics: Max component CFL number: 154.026 +Time: 1.0635e+08s, dt:381746s, Cycle: 748 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.80e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 7.62e-09 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 4.33e-09 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 3.20e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 3.42e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 3.83e-09 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 3.00e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 3.21e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 3.37e-09 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 2.81e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 3.01e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.98e-09 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.64e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 2.82e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.62e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.13e-03 ) ; ( Rwell ) = ( 1.09e-13 ) ; ( R ) = ( 2.13e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.21e-05 ) ; ( Rwell ) = ( 2.64e-16 ) ; ( R ) = ( 4.21e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0735638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652546 +Time: 1.06732e+08s, dt:268395s, Cycle: 749 +well_1Control: BHP (at the specified reference elevation): 27942375.439329714 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; ( R ) = ( 2.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 3.79e-09 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 2.77e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 1.48e-09 ) ; ( R ) = ( 3.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 1.42e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 1.01e-09 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 2.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 8.85e-10 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 5.38e-14 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0520522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0458162 +Time: 1.07e+08s, dt:268395s, Cycle: 750 +well_1Control: BHP (at the specified reference elevation): 27958802.87598205 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 4.78e-08 ) ; ( R ) = ( 2.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 3.75e-09 ) ; ( R ) = ( 7.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 2.14e-09 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 2.72e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 3.16e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 1.88e-09 ) ; ( R ) = ( 6.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.47e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 3.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 1.46e-09 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 1.28e-09 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.13e-09 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 2.29e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 9.99e-10 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.43e-13 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.30e-05 ) ; ( Rwell ) = ( 5.00e-17 ) ; ( R ) = ( 1.30e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0517791 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0456591 +compflowStatistics, reservoir: Pressure (min, average, max): 1.63157e+07, 1.63549e+07, 1.63937e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.80733e+06, 3.88541e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.537 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.61615, 725.92 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2219.77, 702822 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 431.467, 212493 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1788.31, 490329 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 91.9802, 0.476719 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2127.79, 702821 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2219.77, 0 }, { 850.409, 701954 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.62671e+07, 1.63007e+07, 1.63343e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.75871e+06, 3.826e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.497 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0477548, 223.449 } rm^3 +compflowStatistics, caprock: Phase mass: { 18.8519, 216291 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 17.403, 64901.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 1.44894, 151390 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.4742, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 7.37773, 216291 } kg +compflowStatistics, caprock: Dissolved component mass: { { 18.8519, 0 }, { 82.5788, 216207 } } kg +well_1Control: BHP (at the specified reference elevation): 27975162.39615167 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 86.4033 +compflowStatistics: Max component CFL number: 117.885 +Time: 1.07268e+08s, dt:268395s, Cycle: 751 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 4.76e-08 ) ; ( R ) = ( 2.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.36e-08 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.52e-04 ) ; ( Rwell ) = ( 1.71e-12 ) ; ( R ) = ( 9.52e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0517372 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0454182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.07537e+08s, dt:350437s, Cycle: 752 +well_1Control: BHP (at the specified reference elevation): 27991507.366160065 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-02 ) ; ( Rwell ) = ( 6.21e-09 ) ; ( R ) = ( 6.76e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.61e-09 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 2.57e-14 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.24e-04 ) ; ( Rwell ) = ( 3.70e-15 ) ; ( R ) = ( 1.24e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0670672 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0609198 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.07887e+08s, dt:112773s, Cycle: 753 +well_1Control: BHP (at the specified reference elevation): 28012770.7107092 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 1.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.34e-03 ) ; ( Rwell ) = ( 6.85e-10 ) ; ( R ) = ( 9.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.29e-04 ) ; ( Rwell ) = ( 1.13e-14 ) ; ( R ) = ( 8.29e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0222827 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0193907 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08e+08s, dt:217705s, Cycle: 754 +well_1Control: BHP (at the specified reference elevation): 28019681.155770913 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 4.77e-08 ) ; ( R ) = ( 2.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.42e-09 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.68e-03 ) ; ( Rwell ) = ( 2.47e-13 ) ; ( R ) = ( 2.68e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.30e-04 ) ; ( Rwell ) = ( 2.07e-15 ) ; ( R ) = ( 4.30e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0420807 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0370178 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.63451e+07, 1.63844e+07, 1.64232e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.83834e+06, 3.91641e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.558 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.65851, 725.9 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2242.02, 702818 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 433.481, 212504 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1808.54, 490313 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 93.4658, 0.476733 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2148.55, 702817 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2242.02, 0 }, { 853.214, 701947 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.62966e+07, 1.63302e+07, 1.63638e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.78981e+06, 3.85701e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.504 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0507192, 223.453 } rm^3 +compflowStatistics, caprock: Phase mass: { 20.0717, 216300 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 18.3555, 64904.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 1.7162, 151395 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.6111, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 8.46063, 216300 } kg +compflowStatistics, caprock: Dissolved component mass: { { 20.0717, 0 }, { 84.3763, 216214 } } kg +well_1Control: BHP (at the specified reference elevation): 28032961.499514297 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 69.9113 +compflowStatistics: Max component CFL number: 95.39 +Time: 1.08218e+08s, dt:317408s, Cycle: 755 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 4.75e-08 ) ; ( R ) = ( 3.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 5.04e-09 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.19e-03 ) ; ( Rwell ) = ( 3.31e-10 ) ; ( R ) = ( 8.19e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.53e-05 ) ; ( Rwell ) = ( 5.26e-14 ) ; ( R ) = ( 5.53e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0606599 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0538802 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.08535e+08s, dt:374975s, Cycle: 756 +well_1Control: BHP (at the specified reference elevation): 28052196.824886933 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 4.71e-08 ) ; ( R ) = ( 4.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 9.15e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.91e-09 ) ; ( R ) = ( 3.17e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.47e-03 ) ; ( Rwell ) = ( 1.87e-14 ) ; ( R ) = ( 1.47e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.97e-06 ) ; ( Rwell ) = ( 4.58e-15 ) ; ( R ) = ( 6.97e-06 ) ; + Last LinSolve(iter,res) = ( 5, 7.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0711856 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627555 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.0891e+08s, dt:89912.1s, Cycle: 757 +well_1Control: BHP (at the specified reference elevation): 28074773.917135872 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.48e-03 ) ; ( Rwell ) = ( 4.68e-08 ) ; ( R ) = ( 9.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.73e-03 ) ; ( Rwell ) = ( 4.21e-10 ) ; ( R ) = ( 8.73e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 5.74e-14 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.38e-06 ) ; ( Rwell ) = ( 3.78e-15 ) ; ( R ) = ( 3.38e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0178255 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0149672 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.09e+08s, dt:179824s, Cycle: 758 +well_1Control: BHP (at the specified reference elevation): 28080257.239863675 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 1.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.58e-03 ) ; ( Rwell ) = ( 2.43e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 4.17e-10 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.41e-03 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.46e-03 ) ; ( Rwell ) = ( 1.06e-10 ) ; ( R ) = ( 6.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-03 ) ; ( Rwell ) = ( 6.16e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 2.63e-11 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.92e-06 ) ; ( Rwell ) = ( 3.37e-15 ) ; ( R ) = ( 9.92e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.034814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0302877 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.63748e+07, 1.6414e+07, 1.64529e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.86921e+06, 3.94728e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.58 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.70105, 725.879 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2264.46, 702814 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 435.505, 212516 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1828.96, 490298 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 95.0587, 0.476747 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2169.4, 702813 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2264.46, 0 }, { 856.14, 701940 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.63264e+07, 1.63599e+07, 1.63935e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.82081e+06, 3.88788e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.51 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0538014, 223.457 } rm^3 +compflowStatistics, caprock: Phase mass: { 21.3444, 216309 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 19.3254, 64908.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 2.01897, 151400 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.7501, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 9.59427, 216309 } kg +compflowStatistics, caprock: Dissolved component mass: { { 21.3444, 0 }, { 86.1836, 216221 } } kg +well_1Control: BHP (at the specified reference elevation): 28091216.031932205 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 57.6029 +compflowStatistics: Max component CFL number: 78.601 +Time: 1.0918e+08s, dt:289205s, Cycle: 759 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 3.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 4.13e-09 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 1.08e-09 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-04 ) ; ( Rwell ) = ( 5.87e-14 ) ; ( R ) = ( 3.46e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0554892 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0487419 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.09469e+08s, dt:362621s, Cycle: 760 +well_1Control: BHP (at the specified reference elevation): 28108818.817647606 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 4.72e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.64e-02 ) ; ( Rwell ) = ( 6.38e-09 ) ; ( R ) = ( 7.64e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-03 ) ; ( Rwell ) = ( 1.15e-13 ) ; ( R ) = ( 1.66e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-05 ) ; ( Rwell ) = ( 1.58e-15 ) ; ( R ) = ( 1.07e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0690698 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601959 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.09832e+08s, dt:168349s, Cycle: 761 +well_1Control: BHP (at the specified reference elevation): 28130788.23003521 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 4.69e-08 ) ; ( R ) = ( 1.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.00e-03 ) ; ( Rwell ) = ( 3.61e-10 ) ; ( R ) = ( 8.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.00e-04 ) ; ( Rwell ) = ( 4.85e-14 ) ; ( R ) = ( 4.00e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.032554 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0279305 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.1e+08s, dt:280892s, Cycle: 762 +well_1Control: BHP (at the specified reference elevation): 28141016.683768544 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; ( R ) = ( 2.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 3.78e-09 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 9.68e-10 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 1.55e-13 ) ; ( R ) = ( 4.19e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0533859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.046182 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.64088e+07, 1.64481e+07, 1.64869e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.90019e+06, 3.97825e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.604 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.74992, 725.854 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2290.33, 702809 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 437.871, 212529 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1852.46, 490281 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 96.8576, 0.476763 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2193.47, 702809 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2290.33, 0 }, { 859.267, 701933 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.63604e+07, 1.63939e+07, 1.64275e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.85176e+06, 3.91886e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.518 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0574318, 223.46 } rm^3 +compflowStatistics, caprock: Phase mass: { 22.8493, 216318 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 20.4403, 64912.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 2.40903, 151406 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.8475, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 11.0019, 216318 } kg +compflowStatistics, caprock: Dissolved component mass: { { 22.8493, 0 }, { 88.2411, 216228 } } kg +well_1Control: BHP (at the specified reference elevation): 28157964.105236933 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 89.722 +compflowStatistics: Max component CFL number: 122.438 +Time: 1.10281e+08s, dt:363303s, Cycle: 763 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.67e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 6.22e-09 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-03 ) ; ( Rwell ) = ( 1.13e-13 ) ; ( R ) = ( 1.37e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 4.26e-15 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 7, 3.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0685719 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0593272 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.10644e+08s, dt:355805s, Cycle: 764 +well_1Control: BHP (at the specified reference elevation): 28179802.623412706 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.65e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 5.67e-08 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.35e-09 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 3.45e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.96e-09 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 6.47e-13 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 4.85e-15 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0670699 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0580968 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.11e+08s, dt:401298s, Cycle: 765 +well_1Control: BHP (at the specified reference elevation): 28201162.944924098 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 7.37e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.50e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 1.94e-09 ) ; ( R ) = ( 2.25e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 4.95e-10 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 1.23e-13 ) ; ( R ) = ( 5.05e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0756387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0647516 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.64432e+07, 1.64824e+07, 1.65212e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.93086e+06, 4.00892e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.629 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.79891, 725.83 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2316.4, 702805 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 440.206, 212542 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1876.19, 490263 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 98.6517, 0.476779 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2217.75, 702805 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2316.4, 0 }, { 862.669, 701925 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.6395e+07, 1.64283e+07, 1.64618e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.88262e+06, 3.94953e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.526 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0612231, 223.464 } rm^3 +compflowStatistics, caprock: Phase mass: { 24.4272, 216328 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 21.5737, 64916.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 2.85355, 151412 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.8911, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 12.5361, 216328 } kg +compflowStatistics, caprock: Dissolved component mass: { { 24.4272, 0 }, { 90.3154, 216236 } } kg +well_1Control: BHP (at the specified reference elevation): 28225279.54705234 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 127.815 +compflowStatistics: Max component CFL number: 174.435 +Time: 1.11401e+08s, dt:422412s, Cycle: 766 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.63e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 8.15e-09 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 4.62e-13 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 8, 8.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 3.25e-15 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0792563 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664501 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.11824e+08s, dt:176291s, Cycle: 767 +well_1Control: BHP (at the specified reference elevation): 28250585.19333386 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; ( R ) = ( 1.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-03 ) ; ( Rwell ) = ( 2.74e-14 ) ; ( R ) = ( 2.09e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.61e-06 ) ; ( Rwell ) = ( 2.01e-15 ) ; ( R ) = ( 7.61e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0337119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0276989 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.12e+08s, dt:295229s, Cycle: 768 +well_1Control: BHP (at the specified reference elevation): 28261208.644305225 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 2.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 3.98e-09 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.52e-03 ) ; ( Rwell ) = ( 1.24e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.63e-10 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 6.24e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.49e-03 ) ; ( Rwell ) = ( 9.28e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.48e-03 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.98e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 2.31e-10 ) ; ( R ) = ( 6.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.27e-05 ) ; ( Rwell ) = ( 2.09e-14 ) ; ( R ) = ( 8.27e-05 ) ; + Last LinSolve(iter,res) = ( 8, 7.17e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0556282 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0474966 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.64705e+07, 1.65098e+07, 1.65486e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.96151e+06, 4.03957e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.649 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.83794, 725.811 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2337.25, 702802 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 442.071, 212552 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1895.18, 490249 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 99.9937, 0.476792 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2237.26, 702801 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2337.25, 0 }, { 865.31, 701919 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.64224e+07, 1.64557e+07, 1.64892e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.91334e+06, 3.98018e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.532 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0643217, 223.467 } rm^3 +compflowStatistics, caprock: Phase mass: { 25.7217, 216336 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 22.4774, 64919.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 3.24432, 151416 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.9136, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 13.8081, 216336 } kg +compflowStatistics, caprock: Dissolved component mass: { { 25.7217, 0 }, { 91.96, 216242 } } kg +well_1Control: BHP (at the specified reference elevation): 28278919.96880781 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 93.8184 +compflowStatistics: Max component CFL number: 128.045 +Time: 1.12295e+08s, dt:375761s, Cycle: 769 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 4.61e-08 ) ; ( R ) = ( 3.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 6.15e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 4.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.65e-09 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.34e-04 ) ; ( Rwell ) = ( 3.02e-13 ) ; ( R ) = ( 3.34e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0704827 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059339 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.12671e+08s, dt:329010s, Cycle: 770 +well_1Control: BHP (at the specified reference elevation): 28301435.58568579 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 4.81e-09 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 2.42e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.24e-09 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.80e-04 ) ; ( Rwell ) = ( 1.45e-13 ) ; ( R ) = ( 3.80e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.60e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28321141.46474544 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0617703 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518193 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13e+08s, dt:397908s, Cycle: 771 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 2.47e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 1.80e-09 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 1.75e-13 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.59e-06 ) ; ( Rwell ) = ( 3.39e-15 ) ; ( R ) = ( 6.59e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0742303 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619254 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.65042e+07, 1.65435e+07, 1.65823e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 3.99211e+06, 4.07017e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.674 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.88587, 725.788 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2362.96, 702798 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 444.412, 212565 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1918.55, 490232 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 101.907, 0.476809 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2261.05, 702797 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2362.96, 0 }, { 868.547, 701911 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.64562e+07, 1.64894e+07, 1.65229e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.944e+06, 4.01078e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.539 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0682339, 223.471 } rm^3 +compflowStatistics, caprock: Phase mass: { 27.362, 216345 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 23.5923, 64923.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 3.76972, 151422 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.9453, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 15.4168, 216345 } kg +compflowStatistics, caprock: Dissolved component mass: { { 27.362, 0 }, { 93.9762, 216250 } } kg +well_1Control: BHP (at the specified reference elevation): 28344868.153674882 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 126.096 +compflowStatistics: Max component CFL number: 172.112 +Time: 1.13398e+08s, dt:431056s, Cycle: 772 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 8.09e-09 ) ; ( R ) = ( 5.09e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.10e-09 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.81e-03 ) ; ( Rwell ) = ( 5.08e-13 ) ; ( R ) = ( 1.81e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.22e-06 ) ; ( Rwell ) = ( 8.29e-15 ) ; ( R ) = ( 7.22e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0803739 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672473 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13829e+08s, dt:171036s, Cycle: 773 +well_1Control: BHP (at the specified reference elevation): 28370600.065362938 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 1.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 4.77e-09 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.57e-03 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.00e-03 ) ; ( Rwell ) = ( 3.89e-09 ) ; ( R ) = ( 8.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.37e-04 ) ; ( Rwell ) = ( 1.15e-12 ) ; ( R ) = ( 4.37e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.34e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28380883.823169835 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0325341 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0266873 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14e+08s, dt:291126s, Cycle: 774 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 4.60e-08 ) ; ( R ) = ( 2.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 9.47e-10 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 5.31e-10 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 9.14e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 4.68e-10 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 8.56e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 1.58e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 4.14e-10 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 8.02e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.48e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 3.67e-10 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 7.51e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.20e-10 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 7.04e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 1.05e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.30e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 2.83e-10 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 6.59e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 9.80e-09 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 2.49e-10 ) ; ( R ) = ( 6.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.17e-04 ) ; ( Rwell ) = ( 3.50e-14 ) ; ( R ) = ( 4.17e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0545037 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0447408 +well_1Control: BHP (at the specified reference elevation): 28398290.454094842 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.65315e+07, 1.65708e+07, 1.66096e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.02263e+06, 4.10068e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.694 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.92472, 725.769 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2383.87, 702794 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 446.27, 212576 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1937.6, 490219 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 103.148, 0.476822 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2280.72, 702794 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2383.87, 0 }, { 871.062, 701906 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.64835e+07, 1.65167e+07, 1.65502e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 3.97458e+06, 4.0413e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.545 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0714788, 223.474 } rm^3 +compflowStatistics, caprock: Phase mass: { 28.7276, 216353 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 24.4966, 64926.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 4.23095, 151426 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.976, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 16.7516, 216353 } kg +compflowStatistics, caprock: Dissolved component mass: { { 28.7276, 0 }, { 95.5961, 216255 } } kg +compflowStatistics: Max phase CFL number: 92.0498 +compflowStatistics: Max component CFL number: 125.648 +Time: 1.14291e+08s, dt:291126s, Cycle: 775 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 2.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 3.62e-09 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 2.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 9.33e-10 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 8.21e-10 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 1.13e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.68e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 2.09e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 7.23e-10 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.06e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 6.34e-10 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.87e-04 ) ; ( Rwell ) = ( 1.34e-13 ) ; ( R ) = ( 6.87e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0544771 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0448267 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14582e+08s, dt:382932s, Cycle: 776 +well_1Control: BHP (at the specified reference elevation): 28415670.41339244 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; ( R ) = ( 3.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 6.19e-09 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.02e-03 ) ; ( Rwell ) = ( 6.46e-13 ) ; ( R ) = ( 5.02e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.89e-04 ) ; ( Rwell ) = ( 6.29e-15 ) ; ( R ) = ( 3.89e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0710535 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.058376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14965e+08s, dt:34816.1s, Cycle: 777 +well_1Control: BHP (at the specified reference elevation): 28438420.403624028 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.33e-03 ) ; ( Rwell ) = ( 4.53e-08 ) ; ( R ) = ( 3.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.92e-03 ) ; ( Rwell ) = ( 6.50e-11 ) ; ( R ) = ( 2.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-05 ) ; ( Rwell ) = ( 2.10e-14 ) ; ( R ) = ( 2.21e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00708436 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0053334 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.15e+08s, dt:69632.2s, Cycle: 778 +well_1Control: BHP (at the specified reference elevation): 28440504.889180623 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.64e-03 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.97e-03 ) ; ( Rwell ) = ( 2.16e-10 ) ; ( R ) = ( 4.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.41e-04 ) ; ( Rwell ) = ( 2.72e-13 ) ; ( R ) = ( 6.41e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0135165 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0107015 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.65552e+07, 1.65945e+07, 1.66333e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.05311e+06, 4.13116e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.711 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.95842, 725.752 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2402.07, 702792 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 447.832, 212585 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1954.23, 490207 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 104.347, 0.476833 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2297.72, 702791 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2402.07, 0 }, { 873.264, 701900 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.65072e+07, 1.65405e+07, 1.65739e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.00512e+06, 4.07178e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.55 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0743568, 223.476 } rm^3 +compflowStatistics, caprock: Phase mass: { 29.9424, 216359 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 25.2835, 64929.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 4.65889, 151430 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.9656, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 17.9768, 216359 } kg +compflowStatistics, caprock: Dissolved component mass: { { 29.9424, 0 }, { 97.0005, 216261 } } kg +well_1Control: BHP (at the specified reference elevation): 28444671.653397873 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 21.9738 +compflowStatistics: Max component CFL number: 29.9959 +Time: 1.1507e+08s, dt:139264s, Cycle: 779 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 4.56e-08 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 8.29e-10 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.98e-03 ) ; ( Rwell ) = ( 1.17e-13 ) ; ( R ) = ( 1.98e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.04e-06 ) ; ( Rwell ) = ( 3.71e-15 ) ; ( R ) = ( 3.04e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0263212 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0211968 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15209e+08s, dt:260207s, Cycle: 780 +well_1Control: BHP (at the specified reference elevation): 28452972.2260578 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 4.54e-08 ) ; ( R ) = ( 2.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 7.41e-10 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 6.53e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 5.72e-10 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.62e-04 ) ; ( Rwell ) = ( 5.93e-14 ) ; ( R ) = ( 3.62e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0483996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0405597 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15469e+08s, dt:361591s, Cycle: 781 +well_1Control: BHP (at the specified reference elevation): 28468433.082354024 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 4.53e-08 ) ; ( R ) = ( 3.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 2.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 1.39e-09 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-03 ) ; ( Rwell ) = ( 7.86e-14 ) ; ( R ) = ( 2.18e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-05 ) ; ( Rwell ) = ( 3.22e-15 ) ; ( R ) = ( 1.10e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0667157 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0556302 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15831e+08s, dt:169306s, Cycle: 782 +well_1Control: BHP (at the specified reference elevation): 28489827.634007588 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 4.50e-08 ) ; ( R ) = ( 1.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 2.98e-10 ) ; ( R ) = ( 7.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.43e-04 ) ; ( Rwell ) = ( 2.43e-14 ) ; ( R ) = ( 8.43e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0317729 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0259984 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.16e+08s, dt:291436s, Cycle: 783 +well_1Control: BHP (at the specified reference elevation): 28499885.339924596 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 4.52e-08 ) ; ( R ) = ( 2.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.43e-09 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 8.84e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.61e-03 ) ; ( Rwell ) = ( 2.27e-10 ) ; ( R ) = ( 7.61e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.02e-04 ) ; ( Rwell ) = ( 4.75e-14 ) ; ( R ) = ( 5.02e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0538711 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0445703 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.65923e+07, 1.66315e+07, 1.66703e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.08347e+06, 4.16152e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.738 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.0109, 725.727 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2430.52, 702787 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 450.278, 212599 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1980.25, 490188 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 106.52, 0.476852 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2324, 702787 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2430.52, 0 }, { 876.791, 701893 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.65444e+07, 1.65776e+07, 1.6611e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.03558e+06, 4.10214e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.559 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0789633, 223.48 } rm^3 +compflowStatistics, caprock: Phase mass: { 31.8936, 216370 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 26.5137, 64934 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 5.37995, 151436 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.9268, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 19.9668, 216370 } kg +compflowStatistics, caprock: Dissolved component mass: { { 31.8936, 0 }, { 99.1892, 216268 } } kg +well_1Control: BHP (at the specified reference elevation): 28517122.157115087 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 91.6896 +compflowStatistics: Max component CFL number: 125.173 +Time: 1.16291e+08s, dt:384575s, Cycle: 784 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 3.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 5.88e-09 ) ; ( R ) = ( 1.38e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 2.39e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.41e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 3.38e-09 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 8.68e-10 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.71e-04 ) ; ( Rwell ) = ( 2.61e-13 ) ; ( R ) = ( 2.71e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0706863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0579015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.16676e+08s, dt:323989s, Cycle: 785 +well_1Control: BHP (at the specified reference elevation): 28539810.04585725 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; ( R ) = ( 3.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.72e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; ( R ) = ( 7.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 3.38e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 2.39e-09 ) ; ( R ) = ( 4.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 1.75e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 2.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 1.84e-09 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.24e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.78e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.62e-09 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 1.26e-09 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.30e-03 ) ; ( Rwell ) = ( 9.55e-14 ) ; ( R ) = ( 2.30e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.48e-04 ) ; ( Rwell ) = ( 3.66e-15 ) ; ( R ) = ( 3.48e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0597908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0487157 +Time: 1.17e+08s, dt:323989s, Cycle: 786 +well_1Control: BHP (at the specified reference elevation): 28558976.16717823 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 3.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.35e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 3.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 9.74e-09 ) ; ( R ) = ( 6.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 2.56e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 3.18e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.85e-02 ) ; ( Rwell ) = ( 9.53e-09 ) ; ( R ) = ( 8.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.64e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 2.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 9.27e-09 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.99e-03 ) ; ( Rwell ) = ( 4.00e-13 ) ; ( R ) = ( 1.99e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 2.56e-16 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0597568 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0487774 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.66235e+07, 1.66628e+07, 1.67016e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.11371e+06, 4.19176e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.76 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.05504, 725.705 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2454.56, 702784 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 452.425, 212611 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2002.14, 490173 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 108.151, 0.476866 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2346.41, 702783 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2454.56, 0 }, { 879.75, 701886 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.65757e+07, 1.66088e+07, 1.66422e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.06593e+06, 4.13238e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.566 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0829452, 223.483 } rm^3 +compflowStatistics, caprock: Phase mass: { 33.5871, 216378 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 27.5506, 64937.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 6.03643, 151440 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.8613, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 21.7258, 216378 } kg +compflowStatistics, caprock: Dissolved component mass: { { 33.5871, 0 }, { 101.027, 216275 } } kg +well_1Control: BHP (at the specified reference elevation): 28578149.78482055 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 101.672 +compflowStatistics: Max component CFL number: 138.81 +Time: 1.17324e+08s, dt:406063s, Cycle: 787 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 4.48e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.57e-02 ) ; ( Rwell ) = ( 6.49e-09 ) ; ( R ) = ( 8.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.69e-09 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 9.17e-10 ) ; ( R ) = ( 1.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 2.62e-13 ) ; ( R ) = ( 1.64e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.73e-06 ) ; ( Rwell ) = ( 1.49e-15 ) ; ( R ) = ( 2.73e-06 ) ; + Last LinSolve(iter,res) = ( 6, 6.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0742829 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0603395 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.1773e+08s, dt:269948s, Cycle: 788 +well_1Control: BHP (at the specified reference elevation): 28602041.796517663 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; ( R ) = ( 2.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 2.84e-09 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.40e-03 ) ; ( Rwell ) = ( 2.31e-13 ) ; ( R ) = ( 3.40e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.00e-04 ) ; ( Rwell ) = ( 5.99e-15 ) ; ( R ) = ( 7.00e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0496136 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.039834 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18e+08s, dt:378765s, Cycle: 789 +well_1Control: BHP (at the specified reference elevation): 28617933.33459992 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 4.45e-08 ) ; ( R ) = ( 3.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 5.45e-09 ) ; ( R ) = ( 1.81e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.07e-02 ) ; ( Rwell ) = ( 2.36e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 4.17e-09 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 2.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 2.40e-09 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 1.10e-13 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.52e-06 ) ; ( Rwell ) = ( 2.96e-15 ) ; ( R ) = ( 5.52e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0691242 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0556891 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 28640165.488864724 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.66553e+07, 1.66945e+07, 1.67333e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.14389e+06, 4.22194e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.783 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.09978, 725.684 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2479.04, 702780 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 454.571, 212623 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2024.47, 490157 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 110.005, 0.476882 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2369.04, 702780 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2479.04, 0 }, { 882.823, 701880 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.66076e+07, 1.66406e+07, 1.66739e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.09619e+06, 4.16256e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.573 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0870875, 223.486 } rm^3 +compflowStatistics, caprock: Phase mass: { 35.3552, 216386 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 28.6045, 64941.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 6.75073, 151445 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.845, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 23.5102, 216386 } kg +compflowStatistics, caprock: Dissolved component mass: { { 35.3552, 0 }, { 102.896, 216281 } } kg +compflowStatistics: Max phase CFL number: 118.555 +compflowStatistics: Max component CFL number: 161.87 +Time: 1.18379e+08s, dt:438534s, Cycle: 790 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 7.31e-09 ) ; ( R ) = ( 4.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.52e-04 ) ; ( Rwell ) = ( 5.01e-13 ) ; ( R ) = ( 8.52e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0800063 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646726 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18817e+08s, dt:182701s, Cycle: 791 +well_1Control: BHP (at the specified reference elevation): 28665920.449184462 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; ( R ) = ( 1.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 3.33e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.34e-04 ) ; ( Rwell ) = ( 9.92e-13 ) ; ( R ) = ( 5.34e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0339245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0267499 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.19e+08s, dt:310665s, Cycle: 792 +well_1Control: BHP (at the specified reference elevation): 28676731.518169954 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 4.46e-08 ) ; ( R ) = ( 2.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 3.67e-09 ) ; ( R ) = ( 6.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 2.08e-09 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 5.34e-10 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.31e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 1.52e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.12e-10 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 7.71e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.14e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.33e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 3.62e-10 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 7.22e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 1.25e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.27e-03 ) ; ( Rwell ) = ( 3.14e-10 ) ; ( R ) = ( 8.27e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.46e-05 ) ; ( Rwell ) = ( 6.51e-14 ) ; ( R ) = ( 7.46e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0569692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0449828 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.66834e+07, 1.67226e+07, 1.67614e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.17401e+06, 4.25206e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.804 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.13945, 725.664 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2500.81, 702777 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 456.547, 212634 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2044.26, 490144 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 111.403, 0.476897 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2389.4, 702777 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2500.81, 0 }, { 885.368, 701874 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.66357e+07, 1.66687e+07, 1.67021e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.12636e+06, 4.19268e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.579 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0908161, 223.488 } rm^3 +compflowStatistics, caprock: Phase mass: { 36.9527, 216394 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 29.5326, 64944.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 7.42006, 151449 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.7758, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 25.1769, 216394 } kg +compflowStatistics, caprock: Dissolved component mass: { { 36.9527, 0 }, { 104.542, 216287 } } kg +well_1Control: BHP (at the specified reference elevation): 28695043.70037754 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 97.0182 +compflowStatistics: Max component CFL number: 132.474 +Time: 1.19311e+08s, dt:407836s, Cycle: 793 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 4.44e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 6.17e-09 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 2.37e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.59e-09 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.69e-04 ) ; ( Rwell ) = ( 4.09e-13 ) ; ( R ) = ( 9.69e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0741107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.058967 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.19719e+08s, dt:281499s, Cycle: 794 +well_1Control: BHP (at the specified reference elevation): 28718934.386950158 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; ( R ) = ( 2.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 2.92e-09 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 6.04e-13 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.63e-04 ) ; ( Rwell ) = ( 4.24e-15 ) ; ( R ) = ( 1.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0513614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0404642 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2e+08s, dt:391674s, Cycle: 795 +well_1Control: BHP (at the specified reference elevation): 28735425.179573454 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 4.40e-08 ) ; ( R ) = ( 3.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 5.60e-09 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.44e-09 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.40e-03 ) ; ( Rwell ) = ( 1.20e-13 ) ; ( R ) = ( 2.40e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.70e-05 ) ; ( Rwell ) = ( 6.09e-15 ) ; ( R ) = ( 2.70e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0710069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0558496 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.67158e+07, 1.67551e+07, 1.67939e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.2041e+06, 4.28214e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.828 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.18508, 725.642 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2525.94, 702774 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 458.655, 212646 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2067.29, 490128 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 113.117, 0.476912 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2412.83, 702773 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2525.94, 0 }, { 888.403, 701867 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.66683e+07, 1.67012e+07, 1.67345e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.1565e+06, 4.22277e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.586 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0952167, 223.491 } rm^3 +compflowStatistics, caprock: Phase mass: { 38.8444, 216402 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 30.6045, 64948.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 8.23997, 151454 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.6946, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 27.1498, 216402 } kg +compflowStatistics, caprock: Dissolved component mass: { { 38.8444, 0 }, { 106.44, 216294 } } kg +well_1Control: BHP (at the specified reference elevation): 28758322.803158887 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 121.997 +compflowStatistics: Max component CFL number: 166.592 +Time: 1.20392e+08s, dt:452680s, Cycle: 796 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.36e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 8.36e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 2.62e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 3.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 2.53e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.77e-03 ) ; ( Rwell ) = ( 8.18e-12 ) ; ( R ) = ( 1.77e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.48e-06 ) ; ( Rwell ) = ( 4.06e-15 ) ; ( R ) = ( 4.48e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0816904 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641763 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.20844e+08s, dt:155646s, Cycle: 797 +well_1Control: BHP (at the specified reference elevation): 28784725.12000844 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; ( R ) = ( 1.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 8.94e-10 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.99e-03 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 2.23e-10 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 1.28e-13 ) ; ( R ) = ( 4.90e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0287429 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0220544 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.21e+08s, dt:286443s, Cycle: 798 +well_1Control: BHP (at the specified reference elevation): 28793848.186202355 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.39e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 2.91e-09 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.64e-09 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.49e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 9.38e-10 ) ; ( R ) = ( 3.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.27e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 2.34e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 8.24e-10 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 2.19e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 7.24e-10 ) ; ( R ) = ( 4.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 1.11e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 6.36e-10 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.80e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 5.61e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 9.78e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.45e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 1.69e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 4.98e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.39e-05 ) ; ( Rwell ) = ( 1.03e-14 ) ; ( R ) = ( 5.39e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0518841 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0404898 +compflowStatistics, reservoir: Pressure (min, average, max): 1.67426e+07, 1.67819e+07, 1.68207e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.23406e+06, 4.3121e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.847 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.22268, 725.624 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2546.74, 702771 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 460.392, 212656 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2086.34, 490115 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 114.614, 0.476926 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2432.12, 702771 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2546.74, 0 }, { 890.91, 701862 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.66951e+07, 1.6728e+07, 1.67613e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.18655e+06, 4.25272e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.592 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.0989242, 223.493 } rm^3 +compflowStatistics, caprock: Phase mass: { 40.4437, 216409 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 31.4907, 64951.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 8.95292, 151457 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.6609, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 28.7827, 216409 } kg +compflowStatistics, caprock: Dissolved component mass: { { 40.4437, 0 }, { 107.997, 216299 } } kg +well_1Control: BHP (at the specified reference elevation): 28810548.76833094 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 89.0279 +compflowStatistics: Max component CFL number: 121.578 +Time: 1.21286e+08s, dt:286443s, Cycle: 799 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.36e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.90e-09 ) ; ( R ) = ( 4.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 2.25e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 7.40e-10 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 1.70e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 6.52e-10 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 1.59e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 5.73e-10 ) ; ( R ) = ( 1.87e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 2.64e-13 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.27e-06 ) ; ( Rwell ) = ( 3.55e-15 ) ; ( R ) = ( 2.27e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0517301 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0404832 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.21573e+08s, dt:398453s, Cycle: 800 +well_1Control: BHP (at the specified reference elevation): 28827202.77213273 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; ( R ) = ( 3.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.47e-09 ) ; ( R ) = ( 3.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 1.43e-09 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 1.19e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.74e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 8.12e-10 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.76e-04 ) ; ( Rwell ) = ( 1.92e-13 ) ; ( R ) = ( 4.76e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0715157 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0556341 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.21971e+08s, dt:28660.4s, Cycle: 801 +well_1Control: BHP (at the specified reference elevation): 28850307.458054326 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.48e-03 ) ; ( Rwell ) = ( 4.33e-08 ) ; ( R ) = ( 2.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 2.82e-11 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.93e-05 ) ; ( Rwell ) = ( 3.98e-15 ) ; ( R ) = ( 7.93e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00586032 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00400453 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.22e+08s, dt:57320.9s, Cycle: 802 +well_1Control: BHP (at the specified reference elevation): 28851986.256052867 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 4.38e-08 ) ; ( R ) = ( 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 1.18e-10 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.54e-04 ) ; ( Rwell ) = ( 1.47e-13 ) ; ( R ) = ( 5.54e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0108726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00797875 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.67656e+07, 1.68049e+07, 1.68437e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.26389e+06, 4.34193e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.864 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.25486, 725.609 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2564.59, 702769 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 461.898, 212665 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2102.69, 490104 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 115.92, 0.476937 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2448.67, 702768 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2564.59, 0 }, { 893.114, 701858 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.67182e+07, 1.6751e+07, 1.67843e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.21651e+06, 4.28256e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.597 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.102157, 223.495 } rm^3 +compflowStatistics, caprock: Phase mass: { 41.8421, 216415 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 32.2511, 64954.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 9.59097, 151461 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.6834, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 30.1587, 216415 } kg +compflowStatistics, caprock: Dissolved component mass: { { 41.8421, 0 }, { 109.335, 216304 } } kg +well_1Control: BHP (at the specified reference elevation): 28855345.47682522 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 17.7828 +compflowStatistics: Max component CFL number: 24.2857 +Time: 1.22057e+08s, dt:114642s, Cycle: 803 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.92e-03 ) ; ( Rwell ) = ( 4.38e-08 ) ; ( R ) = ( 9.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 4.67e-10 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.27e-03 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 1.18e-10 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.76e-05 ) ; ( Rwell ) = ( 3.28e-14 ) ; ( R ) = ( 5.76e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0212118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0161714 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.22172e+08s, dt:229284s, Cycle: 804 +well_1Control: BHP (at the specified reference elevation): 28862056.48680581 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 4.37e-08 ) ; ( R ) = ( 1.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 2.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 4.72e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.43e-13 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.67e-06 ) ; ( Rwell ) = ( 5.74e-16 ) ; ( R ) = ( 5.67e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.041493 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0325402 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.22401e+08s, dt:356451s, Cycle: 805 +well_1Control: BHP (at the specified reference elevation): 28875415.899288073 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 4.35e-08 ) ; ( R ) = ( 3.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 4.34e-09 ) ; ( R ) = ( 3.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.60e-03 ) ; ( Rwell ) = ( 7.49e-13 ) ; ( R ) = ( 3.60e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-04 ) ; ( Rwell ) = ( 9.13e-16 ) ; ( R ) = ( 1.03e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0640086 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.050087 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.22758e+08s, dt:242303s, Cycle: 806 +well_1Control: BHP (at the specified reference elevation): 28896077.698070772 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; ( R ) = ( 2.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 2.00e-09 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.21e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 5.19e-10 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 1.66e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.32e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 4.59e-10 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.73e-05 ) ; ( Rwell ) = ( 5.83e-14 ) ; ( R ) = ( 7.73e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0438622 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.034259 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.23e+08s, dt:367342s, Cycle: 807 +well_1Control: BHP (at the specified reference elevation): 28910184.388645757 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 4.33e-08 ) ; ( R ) = ( 3.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 4.53e-09 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 2.28e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 1.16e-09 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.97e-03 ) ; ( Rwell ) = ( 1.52e-13 ) ; ( R ) = ( 1.97e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 1.12e-14 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0656797 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0512713 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.68047e+07, 1.68439e+07, 1.68827e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.29378e+06, 4.37181e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.892 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.30957, 725.583 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2595.04, 702765 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 464.549, 212680 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2130.49, 490085 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 118.17, 0.476956 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2476.87, 702764 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2595.04, 0 }, { 896.698, 701850 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.67574e+07, 1.67901e+07, 1.68234e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.2464e+06, 4.31244e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.606 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.107741, 223.498 } rm^3 +compflowStatistics, caprock: Phase mass: { 44.2666, 216425 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 33.5381, 64959.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 10.7285, 151466 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.6617, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 32.6049, 216425 } kg +compflowStatistics, caprock: Dissolved component mass: { { 44.2666, 0 }, { 111.606, 216311 } } kg +well_1Control: BHP (at the specified reference elevation): 28931424.169012774 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s +compflowStatistics: Max phase CFL number: 113.606 +compflowStatistics: Max component CFL number: 155.163 +Time: 1.23367e+08s, dt:447089s, Cycle: 808 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 6.58e-09 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 1.74e-09 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 3.35e-13 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 9, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.64e-05 ) ; ( Rwell ) = ( 4.12e-15 ) ; ( R ) = ( 2.64e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 28957270.136971474 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0797421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0848028 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.23814e+08s, dt:185568s, Cycle: 809 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 2.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 7.41e-09 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 2.18e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 3.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 6.96e-09 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-03 ) ; ( Rwell ) = ( 1.03e-12 ) ; ( R ) = ( 1.68e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.98e-06 ) ; ( Rwell ) = ( 8.02e-15 ) ; ( R ) = ( 3.98e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0337228 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0341687 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.24e+08s, dt:281698s, Cycle: 810 +well_1Control: BHP (at the specified reference elevation): 28968053.453510914 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 4.32e-08 ) ; ( R ) = ( 3.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.63e-09 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 6.75e-10 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.86e-04 ) ; ( Rwell ) = ( 3.49e-14 ) ; ( R ) = ( 7.86e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0505353 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0877631 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.68319e+07, 1.68711e+07, 1.69099e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.3235e+06, 4.40154e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.912 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.3476, 725.564 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2616.3, 702762 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 466.401, 212691 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2149.9, 490072 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 119.476, 0.47697 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2496.82, 702762 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2616.3, 0 }, { 899.172, 701845 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.67846e+07, 1.68174e+07, 1.68506e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.27622e+06, 4.34217e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.612 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.111708, 223.5 } rm^3 +compflowStatistics, caprock: Phase mass: { 45.9956, 216432 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 34.435, 64962.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 11.5605, 151469 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.5787, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 34.4169, 216432 } kg +compflowStatistics, caprock: Dissolved component mass: { { 45.9956, 0 }, { 113.181, 216316 } } kg +well_1Control: BHP (at the specified reference elevation): 28984381.16896478 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 86.931 +compflowStatistics: Max component CFL number: 118.737 +Time: 1.24282e+08s, dt:240938s, Cycle: 811 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 1.90e-09 ) ; ( R ) = ( 4.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 2.20e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 4.88e-10 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 3.44e-14 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.03e-06 ) ; ( Rwell ) = ( 4.23e-15 ) ; ( R ) = ( 1.03e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0433347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0984677 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.24523e+08s, dt:189548s, Cycle: 812 +well_1Control: BHP (at the specified reference elevation): 28998331.66577897 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 4.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 1.17e-09 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.16e-04 ) ; ( Rwell ) = ( 5.40e-13 ) ; ( R ) = ( 9.16e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0341708 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0847055 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.24712e+08s, dt:166262s, Cycle: 813 +well_1Control: BHP (at the specified reference elevation): 29009306.742782027 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.34e-02 ) ; ( Rwell ) = ( 9.03e-10 ) ; ( R ) = ( 3.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 8.17e-13 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.84e-04 ) ; ( Rwell ) = ( 7.93e-16 ) ; ( R ) = ( 2.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0300602 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721725 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.24878e+08s, dt:121554s, Cycle: 814 +well_1Control: BHP (at the specified reference elevation): 29018933.048717022 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 3.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 4.91e-10 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 3.44e-13 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-06 ) ; ( Rwell ) = ( 8.68e-15 ) ; ( R ) = ( 1.87e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0221514 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518891 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25e+08s, dt:146891s, Cycle: 815 +well_1Control: BHP (at the specified reference elevation): 29025978.897078462 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 7.07e-10 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 6.44e-13 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.86e-05 ) ; ( Rwell ) = ( 2.04e-16 ) ; ( R ) = ( 2.86e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29034480.98483352 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0265845 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676735 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.68577e+07, 1.68969e+07, 1.69357e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.35329e+06, 4.43132e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.931 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.38367, 725.547 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2636.5, 702760 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 468.057, 212700 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2168.45, 490059 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 121.013, 0.476982 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2515.49, 702759 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2636.5, 0 }, { 901.403, 701840 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.68104e+07, 1.68431e+07, 1.68763e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.306e+06, 4.37195e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.618 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.115521, 223.502 } rm^3 +compflowStatistics, caprock: Phase mass: { 47.6628, 216438 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 35.2839, 64965.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 12.3789, 151473 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.5553, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 36.1075, 216438 } kg +compflowStatistics, caprock: Dissolved component mass: { { 47.6628, 0 }, { 114.659, 216321 } } kg +compflowStatistics: Max phase CFL number: 45.2373 +compflowStatistics: Max component CFL number: 61.7916 +Time: 1.25147e+08s, dt:150219s, Cycle: 816 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 7.38e-10 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 4.31e-13 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.43e-06 ) ; ( Rwell ) = ( 1.06e-14 ) ; ( R ) = ( 6.43e-06 ) ; + Last LinSolve(iter,res) = ( 8, 7.65e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0272162 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695087 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25297e+08s, dt:150925s, Cycle: 817 +well_1Control: BHP (at the specified reference elevation): 29043186.158455323 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 7.48e-10 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 2.98e-13 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.81e-06 ) ; ( Rwell ) = ( 5.40e-15 ) ; ( R ) = ( 3.81e-06 ) ; + Last LinSolve(iter,res) = ( 6, 8.60e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0273269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065452 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25448e+08s, dt:157758s, Cycle: 818 +well_1Control: BHP (at the specified reference elevation): 29051927.325201623 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.28e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 8.07e-10 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 2.24e-13 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-06 ) ; ( Rwell ) = ( 3.02e-15 ) ; ( R ) = ( 1.19e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.83e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708927 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.25606e+08s, dt:156428s, Cycle: 819 +well_1Control: BHP (at the specified reference elevation): 29061042.725576945 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 4.27e-08 ) ; ( R ) = ( 4.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 1.63e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 6.50e-12 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.37e-06 ) ; ( Rwell ) = ( 9.37e-16 ) ; ( R ) = ( 7.37e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0281641 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695423 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25762e+08s, dt:157113s, Cycle: 820 +well_1Control: BHP (at the specified reference elevation): 29070058.65778771 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 7.79e-10 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 4.19e-13 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-04 ) ; ( Rwell ) = ( 9.43e-15 ) ; ( R ) = ( 2.79e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0282853 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678675 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.25919e+08s, dt:80665.8s, Cycle: 821 +well_1Control: BHP (at the specified reference elevation): 29079115.65202173 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; ( R ) = ( 2.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 2.19e-10 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 7.08e-14 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-06 ) ; ( Rwell ) = ( 1.09e-15 ) ; ( R ) = ( 2.38e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0148701 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0374713 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.26e+08s, dt:116873s, Cycle: 822 +well_1Control: BHP (at the specified reference elevation): 29083770.415809035 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 4.26e-08 ) ; ( R ) = ( 3.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 4.27e-10 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.25e-05 ) ; ( Rwell ) = ( 1.70e-13 ) ; ( R ) = ( 4.25e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0211858 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0573932 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.68865e+07, 1.69257e+07, 1.69645e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.38301e+06, 4.46104e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.952 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.42396, 725.528 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2659.15, 702757 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 469.867, 212711 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2189.28, 490045 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 122.56, 0.476997 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2536.59, 702756 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2659.15, 0 }, { 903.884, 701834 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.68393e+07, 1.6872e+07, 1.69051e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.33578e+06, 4.40167e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.624 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.11985, 223.504 } rm^3 +compflowStatistics, caprock: Phase mass: { 49.5611, 216445 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 36.2308, 64968.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 13.3304, 151477 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.4665, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 38.0946, 216445 } kg +compflowStatistics, caprock: Dissolved component mass: { { 49.5611, 0 }, { 116.316, 216327 } } kg +well_1Control: BHP (at the specified reference elevation): 29090507.72946602 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 35.9109 +compflowStatistics: Max component CFL number: 49.055 +Time: 1.26117e+08s, dt:132820s, Cycle: 823 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 5.46e-10 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.51e-03 ) ; ( Rwell ) = ( 3.91e-13 ) ; ( R ) = ( 5.51e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.19e-05 ) ; ( Rwell ) = ( 3.54e-16 ) ; ( R ) = ( 1.19e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0241243 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662588 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2625e+08s, dt:137727s, Cycle: 824 +well_1Control: BHP (at the specified reference elevation): 29098161.611416023 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.25e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 5.94e-10 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 1.74e-13 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0247903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666277 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.26387e+08s, dt:142297s, Cycle: 825 +well_1Control: BHP (at the specified reference elevation): 29106087.756658416 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.24e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 6.25e-10 ) ; ( R ) = ( 3.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 5.99e-13 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-04 ) ; ( Rwell ) = ( 9.91e-15 ) ; ( R ) = ( 1.04e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.025709 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697326 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.2653e+08s, dt:142660s, Cycle: 826 +well_1Control: BHP (at the specified reference elevation): 29114262.833233193 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 6.24e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 3.90e-13 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-04 ) ; ( Rwell ) = ( 1.00e-14 ) ; ( R ) = ( 1.66e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0255963 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070533 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.26672e+08s, dt:141940s, Cycle: 827 +well_1Control: BHP (at the specified reference elevation): 29122454.35537721 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 6.22e-10 ) ; ( R ) = ( 5.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 2.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.63e-10 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 8.15e-14 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.46e-07 ) ; ( Rwell ) = ( 2.59e-15 ) ; ( R ) = ( 9.46e-07 ) ; + Last LinSolve(iter,res) = ( 5, 2.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0254832 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0678015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.26814e+08s, dt:144975s, Cycle: 828 +well_1Control: BHP (at the specified reference elevation): 29130611.266234048 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 4.23e-08 ) ; ( R ) = ( 4.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 6.42e-10 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.01e-13 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-06 ) ; ( Rwell ) = ( 7.21e-16 ) ; ( R ) = ( 2.01e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0260393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0751582 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.26959e+08s, dt:40708.8s, Cycle: 829 +well_1Control: BHP (at the specified reference elevation): 29138921.21646932 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 1.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 4.99e-11 ) ; ( R ) = ( 4.61e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 3.93e-14 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.93e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29141256.18851848 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00775244 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0217938 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27e+08s, dt:75262.1s, Cycle: 830 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 2.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.78e-03 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 8.78e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-03 ) ; ( Rwell ) = ( 1.30e-13 ) ; ( R ) = ( 2.65e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.37e-06 ) ; ( Rwell ) = ( 7.87e-15 ) ; ( R ) = ( 1.37e-06 ) ; + Last LinSolve(iter,res) = ( 3, 7.39e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29145566.90980147 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0137147 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0420725 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.69148e+07, 1.69541e+07, 1.69929e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.4126e+06, 4.49063e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.972 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.46345, 725.509 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2681.43, 702754 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 471.644, 212722 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2209.78, 490032 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 124.106, 0.477011 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2557.32, 702754 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2681.43, 0 }, { 906.403, 701829 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.68677e+07, 1.69004e+07, 1.69335e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.36548e+06, 4.43127e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.63 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.124181, 223.506 } rm^3 +compflowStatistics, caprock: Phase mass: { 51.4665, 216452 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 37.1622, 64972.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 14.3043, 151480 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.4392, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 40.0272, 216452 } kg +compflowStatistics, caprock: Dissolved component mass: { { 51.4665, 0 }, { 117.948, 216332 } } kg +compflowStatistics: Max phase CFL number: 23.0738 +compflowStatistics: Max component CFL number: 31.5211 +Time: 1.27075e+08s, dt:102534s, Cycle: 831 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; ( R ) = ( 3.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 3.24e-10 ) ; ( R ) = ( 1.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.28e-04 ) ; ( Rwell ) = ( 2.26e-13 ) ; ( R ) = ( 5.28e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0184423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.058383 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27178e+08s, dt:115289s, Cycle: 832 +well_1Control: BHP (at the specified reference elevation): 29151439.87003096 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.09e-10 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 6.55e-14 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-06 ) ; ( Rwell ) = ( 2.19e-15 ) ; ( R ) = ( 3.22e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0207949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27293e+08s, dt:125640s, Cycle: 833 +well_1Control: BHP (at the specified reference elevation): 29158052.10603921 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 2.82e-12 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.07e-06 ) ; ( Rwell ) = ( 9.66e-15 ) ; ( R ) = ( 2.07e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0226145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.063544 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27419e+08s, dt:133871s, Cycle: 834 +well_1Control: BHP (at the specified reference elevation): 29165262.503035106 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 4.22e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 5.35e-10 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.27e-04 ) ; ( Rwell ) = ( 1.67e-13 ) ; ( R ) = ( 8.27e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0239621 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697682 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27553e+08s, dt:134167s, Cycle: 835 +well_1Control: BHP (at the specified reference elevation): 29172929.909590706 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 5.40e-10 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.15e-04 ) ; ( Rwell ) = ( 1.29e-13 ) ; ( R ) = ( 3.15e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0239664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686102 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27687e+08s, dt:135967s, Cycle: 836 +well_1Control: BHP (at the specified reference elevation): 29180593.596702557 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 4.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 5.44e-10 ) ; ( R ) = ( 4.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-03 ) ; ( Rwell ) = ( 7.90e-14 ) ; ( R ) = ( 3.11e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.95e-06 ) ; ( Rwell ) = ( 1.14e-14 ) ; ( R ) = ( 8.95e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0243952 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706389 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.27823e+08s, dt:135144s, Cycle: 837 +well_1Control: BHP (at the specified reference elevation): 29188349.448871225 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 5.34e-10 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 3.26e-15 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.11e-05 ) ; ( Rwell ) = ( 9.37e-15 ) ; ( R ) = ( 3.11e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.17e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0240731 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682529 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27958e+08s, dt:42125.9s, Cycle: 838 +well_1Control: BHP (at the specified reference elevation): 29196067.15039565 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 1.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 6.17e-11 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 1.95e-14 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00797693 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0205356 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28e+08s, dt:79646.5s, Cycle: 839 +well_1Control: BHP (at the specified reference elevation): 29198476.732272383 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.74e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 2.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.66e-05 ) ; ( Rwell ) = ( 1.04e-14 ) ; ( R ) = ( 9.66e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0145308 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.037633 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.69444e+07, 1.69837e+07, 1.70225e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.44207e+06, 4.5201e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 731.994 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.50456, 725.489 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2704.72, 702751 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 473.555, 212734 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2231.16, 490018 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 125.727, 0.477025 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2578.99, 702751 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2704.72, 0 }, { 909.077, 701824 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.68974e+07, 1.693e+07, 1.69631e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.39506e+06, 4.46074e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.637 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.128777, 223.508 } rm^3 +compflowStatistics, caprock: Phase mass: { 53.4948, 216459 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 38.1348, 64975.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 15.36, 151484 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.3719, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 42.1229, 216459 } kg +compflowStatistics, caprock: Dissolved component mass: { { 53.4948, 0 }, { 119.654, 216337 } } kg +well_1Control: BHP (at the specified reference elevation): 29203032.414918534 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 24.3613 +compflowStatistics: Max component CFL number: 33.2819 +Time: 1.2808e+08s, dt:115139s, Cycle: 840 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-02 ) ; ( Rwell ) = ( 3.89e-10 ) ; ( R ) = ( 1.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.48e-04 ) ; ( Rwell ) = ( 2.44e-13 ) ; ( R ) = ( 9.48e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0206499 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0533846 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28195e+08s, dt:136784s, Cycle: 841 +well_1Control: BHP (at the specified reference elevation): 29209610.443117473 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.02e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 4.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 5.55e-10 ) ; ( R ) = ( 3.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 5.88e-13 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-04 ) ; ( Rwell ) = ( 2.02e-16 ) ; ( R ) = ( 2.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.98e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29217423.04471201 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0244207 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656864 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28332e+08s, dt:142644s, Cycle: 842 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.19e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 5.96e-10 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.11e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 1.09e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 8.93e-14 ) ; ( R ) = ( 5.41e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0254137 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708691 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.28474e+08s, dt:141473s, Cycle: 843 +well_1Control: BHP (at the specified reference elevation): 29225552.650660746 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 5.81e-10 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 6.01e-13 ) ; ( R ) = ( 7.02e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0251339 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0765399 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.28616e+08s, dt:133178s, Cycle: 844 +well_1Control: BHP (at the specified reference elevation): 29233615.11389446 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 5.21e-10 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 1.23e-13 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-06 ) ; ( Rwell ) = ( 8.77e-16 ) ; ( R ) = ( 2.26e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0239018 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723374 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.28749e+08s, dt:130278s, Cycle: 845 +well_1Control: BHP (at the specified reference elevation): 29241215.673293218 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 4.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.87e-02 ) ; ( Rwell ) = ( 4.97e-10 ) ; ( R ) = ( 2.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-04 ) ; ( Rwell ) = ( 5.12e-13 ) ; ( R ) = ( 1.94e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0232009 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658185 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28879e+08s, dt:120857s, Cycle: 846 +well_1Control: BHP (at the specified reference elevation): 29248648.439565532 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 4.27e-10 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.56e-04 ) ; ( Rwell ) = ( 1.15e-13 ) ; ( R ) = ( 2.56e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0215409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0519758 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29e+08s, dt:145903s, Cycle: 847 +well_1Control: BHP (at the specified reference elevation): 29255535.790623788 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 1.41e-08 ) ; ( R ) = ( 3.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.39e-04 ) ; ( Rwell ) = ( 5.29e-12 ) ; ( R ) = ( 3.39e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0258972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736927 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.69758e+07, 1.7015e+07, 1.70538e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.47148e+06, 4.54951e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.016 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.54801, 725.468 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2729.41, 702749 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 475.574, 212746 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2253.84, 490003 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 127.488, 0.477041 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2601.92, 702748 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2729.41, 0 }, { 911.917, 701818 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.69288e+07, 1.69613e+07, 1.69944e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.42454e+06, 4.49015e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.644 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.13373, 223.51 } rm^3 +compflowStatistics, caprock: Phase mass: { 55.6884, 216467 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 39.1684, 64979.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 16.52, 151488 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.346, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 44.3425, 216467 } kg +compflowStatistics, caprock: Dissolved component mass: { { 55.6884, 0 }, { 121.451, 216343 } } kg +well_1Control: BHP (at the specified reference elevation): 29263844.267772663 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 44.5176 +compflowStatistics: Max component CFL number: 60.8227 +Time: 1.29146e+08s, dt:140946s, Cycle: 848 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 5.73e-10 ) ; ( R ) = ( 2.53e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 2.10e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 3.13e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 3.25e-10 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 1.25e-13 ) ; ( R ) = ( 7.84e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0250842 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0737979 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.29287e+08s, dt:136026s, Cycle: 849 +well_1Control: BHP (at the specified reference elevation): 29271885.176439635 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 4.17e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 5.24e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-03 ) ; ( Rwell ) = ( 7.76e-14 ) ; ( R ) = ( 1.67e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.34e-05 ) ; ( Rwell ) = ( 6.14e-15 ) ; ( R ) = ( 3.34e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29279620.82933938 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0242832 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695407 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29423e+08s, dt:136623s, Cycle: 850 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 5.24e-10 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 1.26e-13 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.20e-06 ) ; ( Rwell ) = ( 1.29e-14 ) ; ( R ) = ( 8.20e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0242406 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641967 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29559e+08s, dt:144616s, Cycle: 851 +well_1Control: BHP (at the specified reference elevation): 29287385.3262867 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 5.89e-10 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-03 ) ; ( Rwell ) = ( 1.50e-13 ) ; ( R ) = ( 3.91e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.76e-06 ) ; ( Rwell ) = ( 4.24e-15 ) ; ( R ) = ( 9.76e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0256159 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695145 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29704e+08s, dt:145288s, Cycle: 852 +well_1Control: BHP (at the specified reference elevation): 29295595.736794606 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 5.94e-10 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.51e-03 ) ; ( Rwell ) = ( 1.09e-13 ) ; ( R ) = ( 3.51e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 1.04e-14 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0258302 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631783 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.29849e+08s, dt:150599s, Cycle: 853 +well_1Control: BHP (at the specified reference elevation): 29303851.49879141 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 6.35e-10 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-03 ) ; ( Rwell ) = ( 1.43e-13 ) ; ( R ) = ( 1.85e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.26e-05 ) ; ( Rwell ) = ( 1.53e-14 ) ; ( R ) = ( 3.26e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.026673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734092 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3e+08s, dt:145863s, Cycle: 854 +well_1Control: BHP (at the specified reference elevation): 29312417.60803441 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 5.98e-10 ) ; ( R ) = ( 4.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.80e-04 ) ; ( Rwell ) = ( 2.52e-13 ) ; ( R ) = ( 9.80e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0258653 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755819 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.70051e+07, 1.70443e+07, 1.70831e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.50081e+06, 4.57884e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.038 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.58862, 725.449 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2752.58, 702746 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 477.502, 212757 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2275.08, 489989 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 129.429, 0.477055 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2623.15, 702746 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2752.58, 0 }, { 914.544, 701813 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.69582e+07, 1.69907e+07, 1.70238e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.45395e+06, 4.51948e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.65 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.13844, 223.512 } rm^3 +compflowStatistics, caprock: Phase mass: { 57.7813, 216474 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 40.1369, 64982.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 17.6444, 151491 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.3461, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 46.4352, 216474 } kg +compflowStatistics, caprock: Dissolved component mass: { { 57.7813, 0 }, { 123.129, 216348 } } kg +well_1Control: BHP (at the specified reference elevation): 29320713.56119658 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 44.4039 +compflowStatistics: Max component CFL number: 60.6708 +Time: 1.30146e+08s, dt:138500s, Cycle: 855 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 5.37e-10 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.32e-03 ) ; ( Rwell ) = ( 1.87e-13 ) ; ( R ) = ( 1.32e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.23e-06 ) ; ( Rwell ) = ( 1.58e-14 ) ; ( R ) = ( 4.23e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695072 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.30284e+08s, dt:139153s, Cycle: 856 +well_1Control: BHP (at the specified reference elevation): 29328584.15904056 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 5.42e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-04 ) ; ( Rwell ) = ( 2.20e-13 ) ; ( R ) = ( 2.44e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0246313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065216 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.30424e+08s, dt:145796s, Cycle: 857 +well_1Control: BHP (at the specified reference elevation): 29336486.648616187 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 4.14e-08 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 5.93e-10 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-04 ) ; ( Rwell ) = ( 4.24e-13 ) ; ( R ) = ( 4.12e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0261144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664192 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.30569e+08s, dt:150943s, Cycle: 858 +well_1Control: BHP (at the specified reference elevation): 29344763.740678705 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 6.33e-10 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 1.14e-13 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.24e-05 ) ; ( Rwell ) = ( 5.30e-15 ) ; ( R ) = ( 8.24e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0266487 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0747498 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3072e+08s, dt:144411s, Cycle: 859 +well_1Control: BHP (at the specified reference elevation): 29353333.158573344 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 1.47e-08 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.12e-04 ) ; ( Rwell ) = ( 4.30e-12 ) ; ( R ) = ( 6.12e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0255617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.072204 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.30865e+08s, dt:135334s, Cycle: 860 +well_1Control: BHP (at the specified reference elevation): 29361534.89959489 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 5.03e-10 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 3.32e-14 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.96e-05 ) ; ( Rwell ) = ( 1.83e-15 ) ; ( R ) = ( 7.96e-05 ) ; + Last LinSolve(iter,res) = ( 7, 2.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29369215.848928973 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0241697 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0719566 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.31e+08s, dt:132858s, Cycle: 861 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 4.13e-08 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 4.87e-10 ) ; ( R ) = ( 5.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 2.08e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.19e-10 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.59e-05 ) ; ( Rwell ) = ( 4.41e-14 ) ; ( R ) = ( 6.59e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0234725 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716183 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7034e+07, 1.70733e+07, 1.7112e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.53012e+06, 4.60815e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.059 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.62863, 725.43 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2775.47, 702744 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 479.391, 212768 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2296.08, 489976 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 130.889, 0.477069 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2644.58, 702743 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2775.47, 0 }, { 917.08, 701808 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.69872e+07, 1.70196e+07, 1.70527e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.4833e+06, 4.54879e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.657 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.143149, 223.514 } rm^3 +compflowStatistics, caprock: Phase mass: { 59.8804, 216480 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 41.0912, 64986.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 18.7892, 151494 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.3347, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 48.5457, 216480 } kg +compflowStatistics, caprock: Dissolved component mass: { { 59.8804, 0 }, { 124.786, 216353 } } kg +well_1Control: BHP (at the specified reference elevation): 29376750.8988115 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 40.3543 +compflowStatistics: Max component CFL number: 55.1407 +Time: 1.31133e+08s, dt:130842s, Cycle: 862 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 4.63e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 4.28e-13 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.28e-06 ) ; ( Rwell ) = ( 1.75e-15 ) ; ( R ) = ( 5.28e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.41e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29384164.896544874 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0231271 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668111 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31264e+08s, dt:134940s, Cycle: 863 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 4.12e-08 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 4.89e-10 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.29e-10 ) ; ( R ) = ( 4.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 1.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.16e-03 ) ; ( Rwell ) = ( 3.16e-11 ) ; ( R ) = ( 7.16e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.36e-05 ) ; ( Rwell ) = ( 3.75e-14 ) ; ( R ) = ( 4.36e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.023835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660438 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31399e+08s, dt:140223s, Cycle: 864 +well_1Control: BHP (at the specified reference elevation): 29391809.693145793 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 5.29e-10 ) ; ( R ) = ( 2.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.30e-04 ) ; ( Rwell ) = ( 2.02e-13 ) ; ( R ) = ( 5.30e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.02e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29399759.367638126 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0248042 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0724049 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.31539e+08s, dt:137084s, Cycle: 865 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 5.05e-10 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 5.68e-13 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.51e-06 ) ; ( Rwell ) = ( 1.41e-14 ) ; ( R ) = ( 3.51e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0243519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692592 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31676e+08s, dt:138058s, Cycle: 866 +well_1Control: BHP (at the specified reference elevation): 29407525.265746504 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 4.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 5.06e-10 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.63e-04 ) ; ( Rwell ) = ( 3.96e-14 ) ; ( R ) = ( 9.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.67e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29415340.232999742 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0243513 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691955 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31814e+08s, dt:139124s, Cycle: 867 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 5.23e-10 ) ; ( R ) = ( 5.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 2.07e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.52e-05 ) ; ( Rwell ) = ( 2.70e-15 ) ; ( R ) = ( 3.52e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685471 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.31953e+08s, dt:46872s, Cycle: 868 +well_1Control: BHP (at the specified reference elevation): 29423217.998455264 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 1.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-03 ) ; ( Rwell ) = ( 6.02e-11 ) ; ( R ) = ( 3.66e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.36e-04 ) ; ( Rwell ) = ( 3.36e-14 ) ; ( R ) = ( 4.36e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.93e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29425875.29866814 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0087785 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0231678 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32e+08s, dt:84609.7s, Cycle: 869 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.36e-03 ) ; ( Rwell ) = ( 1.90e-10 ) ; ( R ) = ( 7.36e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.06e-03 ) ; ( Rwell ) = ( 1.52e-13 ) ; ( R ) = ( 1.06e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 3.20e-15 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0151815 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0411219 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.70619e+07, 1.71011e+07, 1.71399e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.55938e+06, 4.63741e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.079 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.66714, 725.412 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2797.57, 702741 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 481.22, 212778 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2316.35, 489963 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 132.485, 0.477083 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2665.09, 702741 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2797.57, 0 }, { 919.468, 701803 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.70151e+07, 1.70475e+07, 1.70805e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.5126e+06, 4.57805e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.663 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.147746, 223.515 } rm^3 +compflowStatistics, caprock: Phase mass: { 61.9363, 216487 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 42.0101, 64989.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 19.9263, 151497 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.3264, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 50.61, 216487 } kg +compflowStatistics, caprock: Dissolved component mass: { { 61.9363, 0 }, { 126.38, 216358 } } kg +well_1Control: BHP (at the specified reference elevation): 29430667.127959523 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 25.644 +compflowStatistics: Max component CFL number: 35.0422 +Time: 1.32085e+08s, dt:116708s, Cycle: 870 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 4.11e-08 ) ; ( R ) = ( 3.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 3.60e-10 ) ; ( R ) = ( 2.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 3.01e-13 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-05 ) ; ( Rwell ) = ( 6.48e-15 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0206047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.052418 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32201e+08s, dt:140181s, Cycle: 871 +well_1Control: BHP (at the specified reference elevation): 29437262.53762933 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 4.10e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 5.18e-10 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.04e-03 ) ; ( Rwell ) = ( 6.13e-13 ) ; ( R ) = ( 2.04e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-05 ) ; ( Rwell ) = ( 3.56e-15 ) ; ( R ) = ( 1.53e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639236 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32341e+08s, dt:148791s, Cycle: 872 +well_1Control: BHP (at the specified reference elevation): 29445168.589074768 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 5.98e-09 ) ; ( R ) = ( 5.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 2.06e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 5.65e-09 ) ; ( R ) = ( 4.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 3.76e-11 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 1.53e-14 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0260604 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0748276 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3249e+08s, dt:142251s, Cycle: 873 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 4.09e-08 ) ; ( R ) = ( 4.59e-02 ) ; +well_1Control: BHP (at the specified reference elevation): 29453562.564265803 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 5.30e-10 ) ; ( R ) = ( 2.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 1.61e-13 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.38e-06 ) ; ( Rwell ) = ( 1.14e-15 ) ; ( R ) = ( 5.38e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.41e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0248859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0713855 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.32633e+08s, dt:140399s, Cycle: 874 +well_1Control: BHP (at the specified reference elevation): 29461581.185316354 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 4.08e-08 ) ; ( R ) = ( 4.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 5.13e-10 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.95e-03 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 8.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-04 ) ; ( Rwell ) = ( 2.49e-14 ) ; ( R ) = ( 1.67e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0245635 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664992 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32773e+08s, dt:145241s, Cycle: 875 +well_1Control: BHP (at the specified reference elevation): 29469478.360740826 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 5.39e-10 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 2.05e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 1.38e-10 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.72e-04 ) ; ( Rwell ) = ( 2.64e-14 ) ; ( R ) = ( 8.72e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0254278 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675983 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.32918e+08s, dt:81819.9s, Cycle: 876 +well_1Control: BHP (at the specified reference elevation): 29477653.3169226 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 2.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 1.70e-10 ) ; ( R ) = ( 1.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.48e-05 ) ; ( Rwell ) = ( 3.67e-14 ) ; ( R ) = ( 7.48e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0145557 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0408524 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33e+08s, dt:113261s, Cycle: 877 +well_1Control: BHP (at the specified reference elevation): 29482260.810759082 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 3.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 3.25e-10 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.14e-13 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.61e-06 ) ; ( Rwell ) = ( 1.86e-15 ) ; ( R ) = ( 5.61e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0199707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600861 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 29488633.10844181 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.70918e+07, 1.71311e+07, 1.71698e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.58852e+06, 4.66654e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.101 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.7084, 725.392 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2821.34, 702739 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 483.055, 212790 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2338.29, 489949 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 134.028, 0.477098 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2687.31, 702738 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2821.34, 0 }, { 922.145, 701798 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.70451e+07, 1.70775e+07, 1.71105e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.54184e+06, 4.60718e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.67 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.152779, 223.517 } rm^3 +compflowStatistics, caprock: Phase mass: { 64.1938, 216494 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 43.0032, 64993 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 21.1905, 151501 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.2435, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 52.9502, 216494 } kg +compflowStatistics, caprock: Dissolved component mass: { { 64.1938, 0 }, { 128.088, 216363 } } kg +compflowStatistics: Max phase CFL number: 34.2485 +compflowStatistics: Max component CFL number: 46.8028 +Time: 1.33113e+08s, dt:125069s, Cycle: 878 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 3.99e-10 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-04 ) ; ( Rwell ) = ( 2.96e-13 ) ; ( R ) = ( 6.29e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0219865 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661302 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33238e+08s, dt:129855s, Cycle: 879 +well_1Control: BHP (at the specified reference elevation): 29495664.896680765 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 4.29e-10 ) ; ( R ) = ( 3.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-03 ) ; ( Rwell ) = ( 3.35e-13 ) ; ( R ) = ( 2.74e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-04 ) ; ( Rwell ) = ( 5.26e-16 ) ; ( R ) = ( 1.35e-04 ) ; + Last LinSolve(iter,res) = ( 6, 2.99e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29502957.18700309 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0228675 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627128 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33368e+08s, dt:139540s, Cycle: 880 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 4.93e-10 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.28e-03 ) ; ( Rwell ) = ( 3.00e-13 ) ; ( R ) = ( 2.28e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-05 ) ; ( Rwell ) = ( 7.12e-15 ) ; ( R ) = ( 1.10e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0243529 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0647284 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33508e+08s, dt:146916s, Cycle: 881 +well_1Control: BHP (at the specified reference elevation): 29510790.444362994 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 5.41e-10 ) ; ( R ) = ( 5.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 1.38e-10 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.03e-04 ) ; ( Rwell ) = ( 4.77e-14 ) ; ( R ) = ( 7.03e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0256378 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692803 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33655e+08s, dt:147930s, Cycle: 882 +well_1Control: BHP (at the specified reference elevation): 29519035.003830634 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 5.49e-10 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 3.91e-13 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.59e-06 ) ; ( Rwell ) = ( 9.94e-16 ) ; ( R ) = ( 4.59e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0262903 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671216 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33803e+08s, dt:152099s, Cycle: 883 +well_1Control: BHP (at the specified reference elevation): 29527343.102724288 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 5.84e-10 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.54e-13 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.50e-05 ) ; ( Rwell ) = ( 6.60e-15 ) ; ( R ) = ( 5.50e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0271519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0660952 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33955e+08s, dt:45330.8s, Cycle: 884 +well_1Control: BHP (at the specified reference elevation): 29535889.73686994 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 1.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-03 ) ; ( Rwell ) = ( 5.55e-11 ) ; ( R ) = ( 3.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-04 ) ; ( Rwell ) = ( 1.06e-13 ) ; ( R ) = ( 1.53e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00850006 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0199744 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34e+08s, dt:86580.9s, Cycle: 885 +well_1Control: BHP (at the specified reference elevation): 29538443.544339202 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; ( R ) = ( 2.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 1.84e-10 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 2.35e-13 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.31e-05 ) ; ( Rwell ) = ( 2.83e-15 ) ; ( R ) = ( 2.31e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0152038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0375083 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.71201e+07, 1.71593e+07, 1.71981e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.61757e+06, 4.6956e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.121 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.74727, 725.374 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2843.81, 702737 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 484.866, 212801 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2358.95, 489936 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 135.776, 0.477112 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2708.04, 702736 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2843.81, 0 }, { 924.681, 701793 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.70735e+07, 1.71058e+07, 1.71388e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.57098e+06, 4.63624e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.676 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.157606, 223.518 } rm^3 +compflowStatistics, caprock: Phase mass: { 66.3652, 216500 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 43.9432, 64996.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 22.422, 151504 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.2195, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 55.1457, 216500 } kg +compflowStatistics, caprock: Dissolved component mass: { { 66.3652, 0 }, { 129.689, 216368 } } kg +well_1Control: BHP (at the specified reference elevation): 29543315.70460518 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 26.124 +compflowStatistics: Max component CFL number: 35.7021 +Time: 1.34087e+08s, dt:125379s, Cycle: 886 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; ( R ) = ( 3.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 5.72e-09 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.86e-04 ) ; ( Rwell ) = ( 2.58e-12 ) ; ( R ) = ( 8.86e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0219306 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0505587 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34212e+08s, dt:153868s, Cycle: 887 +well_1Control: BHP (at the specified reference elevation): 29550371.758085065 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 4.06e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 5.95e-10 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 1.66e-13 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-06 ) ; ( Rwell ) = ( 1.47e-14 ) ; ( R ) = ( 1.06e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0276044 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566194 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34366e+08s, dt:176340s, Cycle: 888 +well_1Control: BHP (at the specified reference elevation): 29559018.43286172 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 4.05e-08 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 7.72e-10 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 2.04e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.00e-10 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-04 ) ; ( Rwell ) = ( 2.00e-14 ) ; ( R ) = ( 1.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0863512 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.34542e+08s, dt:152580s, Cycle: 889 +well_1Control: BHP (at the specified reference elevation): 29568902.247671686 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 5.72e-10 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.17e-04 ) ; ( Rwell ) = ( 8.05e-14 ) ; ( R ) = ( 6.17e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0265638 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0799886 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.34695e+08s, dt:139326s, Cycle: 890 +well_1Control: BHP (at the specified reference elevation): 29577454.604096733 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 4.68e-10 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 2.03e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.68e-03 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 7.68e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.41e-05 ) ; ( Rwell ) = ( 4.69e-14 ) ; ( R ) = ( 2.41e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0251372 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736546 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.34834e+08s, dt:134639s, Cycle: 891 +well_1Control: BHP (at the specified reference elevation): 29585256.893571876 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-04 ) ; ( Rwell ) = ( 1.07e-13 ) ; ( R ) = ( 2.82e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0234516 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675044 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34969e+08s, dt:31287.7s, Cycle: 892 +well_1Control: BHP (at the specified reference elevation): 29592792.21634411 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; ( R ) = ( 1.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.10e-03 ) ; ( Rwell ) = ( 2.11e-11 ) ; ( R ) = ( 6.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.83e-04 ) ; ( Rwell ) = ( 1.19e-14 ) ; ( R ) = ( 2.83e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00598558 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0153086 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.35e+08s, dt:62575.3s, Cycle: 893 +well_1Control: BHP (at the specified reference elevation): 29594546.330396023 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 4.03e-08 ) ; ( R ) = ( 2.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.49e-03 ) ; ( Rwell ) = ( 9.40e-11 ) ; ( R ) = ( 8.49e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.42e-05 ) ; ( Rwell ) = ( 1.28e-13 ) ; ( R ) = ( 6.42e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.011251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0289818 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.71484e+07, 1.71877e+07, 1.72264e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.6466e+06, 4.72462e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.142 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.78619, 725.356 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2866.38, 702735 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 486.679, 212811 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2379.7, 489923 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 137.336, 0.477126 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2729.05, 702734 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2866.38, 0 }, { 927.158, 701788 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.71019e+07, 1.71341e+07, 1.71671e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.60005e+06, 4.66527e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.682 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.162501, 223.52 } rm^3 +compflowStatistics, caprock: Phase mass: { 68.5747, 216507 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 44.8829, 64999.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 23.6918, 151507 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.1402, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 57.4345, 216507 } kg +compflowStatistics, caprock: Dissolved component mass: { { 68.5747, 0 }, { 131.29, 216373 } } kg +well_1Control: BHP (at the specified reference elevation): 29598051.628766794 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 18.8399 +compflowStatistics: Max component CFL number: 25.7488 +Time: 1.35063e+08s, dt:102692s, Cycle: 894 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 4.02e-08 ) ; ( R ) = ( 3.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.52e-10 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.61e-04 ) ; ( Rwell ) = ( 2.35e-13 ) ; ( R ) = ( 2.61e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.59e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29603789.513802893 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0179715 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0437033 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35165e+08s, dt:137004s, Cycle: 895 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 4.49e-10 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 5.00e-14 ) ; ( R ) = ( 3.22e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.40e-06 ) ; ( Rwell ) = ( 1.86e-15 ) ; ( R ) = ( 6.40e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0238605 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0631294 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35302e+08s, dt:146596s, Cycle: 896 +well_1Control: BHP (at the specified reference elevation): 29611437.637885872 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 4.01e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 5.18e-10 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 2.89e-14 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-06 ) ; ( Rwell ) = ( 3.91e-15 ) ; ( R ) = ( 1.85e-06 ) ; + Last LinSolve(iter,res) = ( 7, 9.79e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0256055 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0704918 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.35449e+08s, dt:145913s, Cycle: 897 +well_1Control: BHP (at the specified reference elevation): 29619613.999354765 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 5.13e-10 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 2.65e-13 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.05e-07 ) ; ( Rwell ) = ( 7.11e-15 ) ; ( R ) = ( 7.05e-07 ) ; + Last LinSolve(iter,res) = ( 8, 5.71e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0251828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688829 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35595e+08s, dt:147482s, Cycle: 898 +well_1Control: BHP (at the specified reference elevation): 29627751.66937507 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 5.17e-10 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 1.32e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.18e-04 ) ; ( Rwell ) = ( 8.81e-14 ) ; ( R ) = ( 5.18e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0255167 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0693444 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35742e+08s, dt:148408s, Cycle: 899 +well_1Control: BHP (at the specified reference elevation): 29635978.179580264 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 1.50e-09 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.55e-03 ) ; ( Rwell ) = ( 2.22e-13 ) ; ( R ) = ( 3.55e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.01e-06 ) ; ( Rwell ) = ( 1.16e-14 ) ; ( R ) = ( 9.01e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0256986 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662507 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.35891e+08s, dt:109330s, Cycle: 900 +well_1Control: BHP (at the specified reference elevation): 29644252.624026306 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 3.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 2.87e-10 ) ; ( R ) = ( 2.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.01e-04 ) ; ( Rwell ) = ( 6.59e-14 ) ; ( R ) = ( 2.01e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0193487 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0490259 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36e+08s, dt:136621s, Cycle: 901 +well_1Control: BHP (at the specified reference elevation): 29650349.766918965 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 4.40e-10 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.46e-13 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-05 ) ; ( Rwell ) = ( 5.64e-15 ) ; ( R ) = ( 3.43e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0235537 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588936 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 29657969.0460497 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.71794e+07, 1.72187e+07, 1.72575e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.67549e+06, 4.75351e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.165 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.82863, 725.336 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2891.09, 702732 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 488.606, 212823 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2402.48, 489909 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 138.928, 0.477142 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2752.16, 702732 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2891.09, 0 }, { 929.99, 701783 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7133e+07, 1.71652e+07, 1.71981e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.62905e+06, 4.69416e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.689 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.167952, 223.521 } rm^3 +compflowStatistics, caprock: Phase mass: { 71.042, 216513 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 45.9159, 65003.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 25.126, 151510 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.0798, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 59.9622, 216513 } kg +compflowStatistics, caprock: Dissolved component mass: { { 71.042, 0 }, { 133.038, 216378 } } kg +compflowStatistics: Max phase CFL number: 41.036 +compflowStatistics: Max component CFL number: 56.0877 +Time: 1.36137e+08s, dt:152781s, Cycle: 902 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.00e-08 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 5.51e-10 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 1.24e-13 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0267311 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588107 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36289e+08s, dt:171004s, Cycle: 903 +well_1Control: BHP (at the specified reference elevation): 29666479.040136382 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.99e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 6.78e-10 ) ; ( R ) = ( 6.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.75e-10 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 4.61e-14 ) ; ( R ) = ( 8.11e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0296777 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663051 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.3646e+08s, dt:177241s, Cycle: 904 +well_1Control: BHP (at the specified reference elevation): 29676000.281252414 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 7.24e-10 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 1.63e-13 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311794 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661806 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36638e+08s, dt:183932s, Cycle: 905 +well_1Control: BHP (at the specified reference elevation): 29685867.67695751 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 7.83e-10 ) ; ( R ) = ( 3.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.34e-03 ) ; ( Rwell ) = ( 4.40e-13 ) ; ( R ) = ( 5.34e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-05 ) ; ( Rwell ) = ( 5.40e-15 ) ; ( R ) = ( 1.15e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0319978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.063643 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36822e+08s, dt:178421s, Cycle: 906 +well_1Control: BHP (at the specified reference elevation): 29696102.45856417 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 7.32e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 3.17e-13 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-05 ) ; ( Rwell ) = ( 1.59e-14 ) ; ( R ) = ( 1.88e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.94e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29706044.729871567 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0305938 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650521 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.37e+08s, dt:187244s, Cycle: 907 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 8.11e-10 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 2.08e-10 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-03 ) ; ( Rwell ) = ( 1.29e-13 ) ; ( R ) = ( 1.35e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-06 ) ; ( Rwell ) = ( 7.27e-15 ) ; ( R ) = ( 2.84e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0321192 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.071326 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.72098e+07, 1.7249e+07, 1.72878e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.70435e+06, 4.78238e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.187 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.87012, 725.316 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2915.31, 702730 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 490.631, 212835 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2424.68, 489895 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 140.706, 0.477157 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2774.61, 702730 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2915.31, 0 }, { 932.673, 701778 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.71634e+07, 1.71955e+07, 1.72284e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.65796e+06, 4.72302e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.696 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.173352, 223.523 } rm^3 +compflowStatistics, caprock: Phase mass: { 73.4945, 216520 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 46.9266, 65006.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 26.5679, 151513 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.0542, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 62.4403, 216520 } kg +compflowStatistics, caprock: Dissolved component mass: { { 73.4945, 0 }, { 134.742, 216383 } } kg +well_1Control: BHP (at the specified reference elevation): 29716474.445307266 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 56.112 +compflowStatistics: Max component CFL number: 76.6978 +Time: 1.37187e+08s, dt:184909s, Cycle: 908 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 7.90e-10 ) ; ( R ) = ( 8.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 2.01e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 2.01e-10 ) ; ( R ) = ( 1.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 8.77e-14 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0317976 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0752888 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.37372e+08s, dt:176042s, Cycle: 909 +well_1Control: BHP (at the specified reference elevation): 29726767.87348115 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 7.11e-10 ) ; ( R ) = ( 4.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-02 ) ; ( Rwell ) = ( 1.11e-13 ) ; ( R ) = ( 2.70e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 1.19e-14 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.030107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0764926 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.37548e+08s, dt:165791s, Cycle: 910 +well_1Control: BHP (at the specified reference elevation): 29736577.418950707 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.98e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 8.67e-09 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 2.61e-12 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.44e-06 ) ; ( Rwell ) = ( 1.53e-15 ) ; ( R ) = ( 2.44e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284567 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0782336 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.37714e+08s, dt:153735s, Cycle: 911 +well_1Control: BHP (at the specified reference elevation): 29745810.321393944 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 5.46e-10 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 7.98e-15 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.14e-06 ) ; ( Rwell ) = ( 8.81e-15 ) ; ( R ) = ( 4.14e-06 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0263527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0752902 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.37868e+08s, dt:132279s, Cycle: 912 +well_1Control: BHP (at the specified reference elevation): 29754368.270378962 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.97e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.94e-10 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-04 ) ; ( Rwell ) = ( 1.32e-13 ) ; ( R ) = ( 2.82e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0236527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633267 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38e+08s, dt:141256s, Cycle: 913 +well_1Control: BHP (at the specified reference elevation): 29761722.083060578 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 4.43e-10 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 1.09e-13 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.53e-06 ) ; ( Rwell ) = ( 1.16e-14 ) ; ( R ) = ( 4.53e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0248811 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652989 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.72373e+07, 1.72765e+07, 1.73153e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.73322e+06, 4.81124e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.207 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.9078, 725.299 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2937.38, 702728 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 492.413, 212845 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2444.97, 489883 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.114, 0.477171 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2795.27, 702728 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2937.38, 0 }, { 935.014, 701774 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.71909e+07, 1.72231e+07, 1.7256e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.68684e+06, 4.75188e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.702 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.178319, 223.524 } rm^3 +compflowStatistics, caprock: Phase mass: { 75.7579, 216526 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 47.8439, 65010.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 27.9139, 151516 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.031, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 64.7269, 216526 } kg +compflowStatistics, caprock: Dissolved component mass: { { 75.7579, 0 }, { 136.28, 216387 } } kg +well_1Control: BHP (at the specified reference elevation): 29769582.015936263 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 42.2425 +compflowStatistics: Max component CFL number: 57.7429 +Time: 1.38141e+08s, dt:147877s, Cycle: 914 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 3.96e-08 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.88e-10 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-04 ) ; ( Rwell ) = ( 1.76e-13 ) ; ( R ) = ( 1.37e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0260763 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695542 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38289e+08s, dt:148508s, Cycle: 915 +well_1Control: BHP (at the specified reference elevation): 29777801.023513094 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.84e-02 ) ; ( Rwell ) = ( 4.83e-10 ) ; ( R ) = ( 8.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.99e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 2.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 2.75e-10 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 1.58e-13 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.04e-06 ) ; ( Rwell ) = ( 6.73e-15 ) ; ( R ) = ( 3.04e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0257809 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665982 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38438e+08s, dt:153480s, Cycle: 916 +well_1Control: BHP (at the specified reference elevation): 29786043.113515303 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.95e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 5.14e-10 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-04 ) ; ( Rwell ) = ( 6.20e-14 ) ; ( R ) = ( 4.56e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.93e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29794550.3600964 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.026269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618923 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38591e+08s, dt:166323s, Cycle: 917 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; ( R ) = ( 4.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 6.03e-10 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.82e-04 ) ; ( Rwell ) = ( 4.10e-13 ) ; ( R ) = ( 8.82e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284922 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0725403 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.38757e+08s, dt:162394s, Cycle: 918 +well_1Control: BHP (at the specified reference elevation): 29803766.976881884 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.94e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 5.77e-10 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 1.98e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 2.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 3.24e-10 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 1.90e-13 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.72e-06 ) ; ( Rwell ) = ( 4.18e-15 ) ; ( R ) = ( 2.72e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0283927 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0768252 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3892e+08s, dt:80162.5s, Cycle: 919 +well_1Control: BHP (at the specified reference elevation): 29812746.025819376 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 1.44e-14 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.24e-06 ) ; ( Rwell ) = ( 1.98e-14 ) ; ( R ) = ( 6.24e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0140218 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0393467 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39e+08s, dt:113214s, Cycle: 920 +well_1Control: BHP (at the specified reference elevation): 29817178.998778306 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 3.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.23e-03 ) ; ( Rwell ) = ( 2.74e-10 ) ; ( R ) = ( 8.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.68e-04 ) ; ( Rwell ) = ( 2.42e-13 ) ; ( R ) = ( 3.68e-04 ) ; + Last LinSolve(iter,res) = ( 9, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0194683 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0566282 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.72652e+07, 1.73045e+07, 1.73433e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.762e+06, 4.84002e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.227 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.94594, 725.281 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2959.79, 702726 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 494.112, 212856 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2465.68, 489870 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.848, 0.477184 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2815.94, 702726 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2959.79, 0 }, { 937.457, 701770 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7219e+07, 1.7251e+07, 1.72839e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.71569e+06, 4.78066e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.708 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.18344, 223.525 } rm^3 +compflowStatistics, caprock: Phase mass: { 78.0973, 216532 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 48.7778, 65013.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 29.3196, 151519 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9547, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 67.1426, 216532 } kg +compflowStatistics, caprock: Dissolved component mass: { { 78.0973, 0 }, { 137.828, 216391 } } kg +well_1Control: BHP (at the specified reference elevation): 29823436.956398133 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 33.785 +compflowStatistics: Max component CFL number: 46.1844 +Time: 1.39113e+08s, dt:129735s, Cycle: 921 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 3.61e-10 ) ; ( R ) = ( 3.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.29e-04 ) ; ( Rwell ) = ( 6.79e-15 ) ; ( R ) = ( 4.29e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0221637 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632502 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39243e+08s, dt:138648s, Cycle: 922 +well_1Control: BHP (at the specified reference elevation): 29830606.31878078 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 2.53e-09 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.63e-04 ) ; ( Rwell ) = ( 2.14e-12 ) ; ( R ) = ( 3.63e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.02399 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618541 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39382e+08s, dt:150309s, Cycle: 923 +well_1Control: BHP (at the specified reference elevation): 29838261.614607267 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.80e-10 ) ; ( R ) = ( 3.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.09e-03 ) ; ( Rwell ) = ( 2.37e-13 ) ; ( R ) = ( 4.09e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-05 ) ; ( Rwell ) = ( 1.25e-14 ) ; ( R ) = ( 1.85e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0258491 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641157 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39532e+08s, dt:159233s, Cycle: 924 +well_1Control: BHP (at the specified reference elevation): 29846555.96644415 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 5.44e-10 ) ; ( R ) = ( 6.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.31e-05 ) ; ( Rwell ) = ( 1.84e-14 ) ; ( R ) = ( 4.31e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0270664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661134 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39691e+08s, dt:165354s, Cycle: 925 +well_1Control: BHP (at the specified reference elevation): 29855339.76517608 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 5.69e-10 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-03 ) ; ( Rwell ) = ( 2.91e-13 ) ; ( R ) = ( 2.14e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-05 ) ; ( Rwell ) = ( 4.32e-15 ) ; ( R ) = ( 1.00e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0281772 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0656609 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39856e+08s, dt:143507s, Cycle: 926 +well_1Control: BHP (at the specified reference elevation): 29864447.44037988 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 4.35e-10 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 1.92e-13 ) ; ( R ) = ( 5.94e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.024938 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0583167 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4e+08s, dt:161474s, Cycle: 927 +well_1Control: BHP (at the specified reference elevation): 29872364.080801442 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 5.49e-10 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.47e-03 ) ; ( Rwell ) = ( 6.22e-14 ) ; ( R ) = ( 5.47e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.40e-05 ) ; ( Rwell ) = ( 1.17e-14 ) ; ( R ) = ( 2.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29881265.293765873 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.028084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633103 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.72953e+07, 1.73345e+07, 1.73733e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.79065e+06, 4.86867e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.249 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.98679, 725.262 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2983.87, 702724 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 496.025, 212868 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2487.85, 489857 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.651, 0.477199 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2838.22, 702724 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2983.87, 0 }, { 940.148, 701765 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.72491e+07, 1.72811e+07, 1.73139e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.74445e+06, 4.80931e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.715 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.189011, 223.526 } rm^3 +compflowStatistics, caprock: Phase mass: { 80.6501, 216538 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 49.7803, 65017 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 30.8698, 151521 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9268, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 69.7233, 216538 } kg +compflowStatistics, caprock: Dissolved component mass: { { 80.6501, 0 }, { 139.492, 216396 } } kg +compflowStatistics: Max phase CFL number: 48.0781 +compflowStatistics: Max component CFL number: 65.7268 +Time: 1.40161e+08s, dt:172462s, Cycle: 928 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 6.22e-10 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 1.58e-10 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.83e-05 ) ; ( Rwell ) = ( 1.10e-15 ) ; ( R ) = ( 8.83e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 29890790.5781674 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0293132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730363 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.40334e+08s, dt:167615s, Cycle: 929 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 5.90e-10 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 1.51e-10 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 2.34e-14 ) ; ( R ) = ( 4.61e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730186 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.40502e+08s, dt:162931s, Cycle: 930 +well_1Control: BHP (at the specified reference elevation): 29900053.032684315 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.91e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 5.49e-10 ) ; ( R ) = ( 4.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 1.37e-10 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.61e-04 ) ; ( Rwell ) = ( 5.22e-14 ) ; ( R ) = ( 4.61e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0276665 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686568 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.40664e+08s, dt:165042s, Cycle: 931 +well_1Control: BHP (at the specified reference elevation): 29909050.988194633 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 5.67e-10 ) ; ( R ) = ( 5.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 1.97e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 1.45e-10 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 9.87e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 3.56e-11 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-05 ) ; ( Rwell ) = ( 7.94e-15 ) ; ( R ) = ( 2.33e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0279829 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623084 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4083e+08s, dt:170477s, Cycle: 932 +well_1Control: BHP (at the specified reference elevation): 29918153.272882655 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855637e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.90e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 5.93e-10 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 1.49e-10 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 9.85e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 3.78e-11 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 4.94e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.56e-03 ) ; ( Rwell ) = ( 9.32e-12 ) ; ( R ) = ( 2.56e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.07e-06 ) ; ( Rwell ) = ( 1.66e-15 ) ; ( R ) = ( 9.07e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0287742 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640887 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41e+08s, dt:180647s, Cycle: 933 +well_1Control: BHP (at the specified reference elevation): 29927534.075596448 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.89e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 6.55e-09 ) ; ( R ) = ( 6.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 6.11e-09 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.11e-12 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 9.12e-15 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0309312 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0698764 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.73245e+07, 1.73637e+07, 1.74025e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.81932e+06, 4.89734e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.27 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.02653, 725.243 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3007.37, 702722 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 497.915, 212879 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2509.45, 489844 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.127, 0.477214 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2860.24, 702722 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3007.37, 0 }, { 942.666, 701761 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.72783e+07, 1.73103e+07, 1.73431e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.77314e+06, 4.83798e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.721 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.194496, 223.527 } rm^3 +compflowStatistics, caprock: Phase mass: { 83.1718, 216544 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 50.7592, 65020.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 32.4126, 151524 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9157, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 72.2561, 216544 } kg +compflowStatistics, caprock: Dissolved component mass: { { 83.1718, 0 }, { 141.094, 216400 } } kg +well_1Control: BHP (at the specified reference elevation): 29937460.266507275 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 53.6692 +compflowStatistics: Max component CFL number: 73.3742 +Time: 1.41181e+08s, dt:180860s, Cycle: 934 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 3.88e-08 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.25e-02 ) ; ( Rwell ) = ( 6.62e-10 ) ; ( R ) = ( 8.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.96e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 1.69e-10 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-04 ) ; ( Rwell ) = ( 7.08e-14 ) ; ( R ) = ( 2.08e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0306718 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694194 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41362e+08s, dt:181865s, Cycle: 935 +well_1Control: BHP (at the specified reference elevation): 29947374.41961278 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 6.62e-10 ) ; ( R ) = ( 5.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.14e-03 ) ; ( Rwell ) = ( 1.67e-10 ) ; ( R ) = ( 7.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 2.55e-14 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0306089 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0652446 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41543e+08s, dt:190493s, Cycle: 936 +well_1Control: BHP (at the specified reference elevation): 29957333.627842095 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 7.22e-10 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.49e-03 ) ; ( Rwell ) = ( 8.21e-14 ) ; ( R ) = ( 4.49e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.68e-05 ) ; ( Rwell ) = ( 1.06e-15 ) ; ( R ) = ( 7.68e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0322075 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666728 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41734e+08s, dt:196727s, Cycle: 937 +well_1Control: BHP (at the specified reference elevation): 29967767.123575024 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 7.66e-10 ) ; ( R ) = ( 9.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 1.94e-10 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-04 ) ; ( Rwell ) = ( 3.90e-14 ) ; ( R ) = ( 1.70e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0329861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645512 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.41931e+08s, dt:69408.3s, Cycle: 938 +well_1Control: BHP (at the specified reference elevation): 29978522.359396785 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 1.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.14e-03 ) ; ( Rwell ) = ( 9.48e-11 ) ; ( R ) = ( 9.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.97e-04 ) ; ( Rwell ) = ( 2.30e-14 ) ; ( R ) = ( 3.97e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0121383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0231902 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.42e+08s, dt:125242s, Cycle: 939 +well_1Control: BHP (at the specified reference elevation): 29982326.264510117 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 3.10e-10 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.06e-03 ) ; ( Rwell ) = ( 7.59e-11 ) ; ( R ) = ( 7.06e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e-04 ) ; ( Rwell ) = ( 1.94e-14 ) ; ( R ) = ( 1.07e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0221798 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0442039 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.73514e+07, 1.73906e+07, 1.74294e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.84781e+06, 4.92583e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.29 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.06294, 725.227 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3028.99, 702721 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 499.529, 212889 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2529.46, 489832 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.64, 0.477227 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2880.35, 702720 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3028.99, 0 }, { 945.14, 701757 } } kg +well_1Control: BHP (at the specified reference elevation): 29989184.655420728 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.73053e+07, 1.73372e+07, 1.737e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.80175e+06, 4.86647e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.727 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.199623, 223.528 } rm^3 +compflowStatistics, caprock: Phase mass: { 85.5352, 216550 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 51.6621, 65023.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 33.8732, 151526 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8534, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 74.6818, 216550 } kg +compflowStatistics, caprock: Dissolved component mass: { { 85.5352, 0 }, { 142.564, 216404 } } kg +compflowStatistics: Max phase CFL number: 37.1342 +compflowStatistics: Max component CFL number: 50.7707 +Time: 1.42125e+08s, dt:166033s, Cycle: 940 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 5.40e-10 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.41e-10 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.13e-04 ) ; ( Rwell ) = ( 7.67e-15 ) ; ( R ) = ( 5.13e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0286247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676469 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.42291e+08s, dt:169839s, Cycle: 941 +well_1Control: BHP (at the specified reference elevation): 29998275.45803769 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 5.67e-10 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.93e-13 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.27e-06 ) ; ( Rwell ) = ( 6.19e-15 ) ; ( R ) = ( 8.27e-06 ) ; + Last LinSolve(iter,res) = ( 5, 8.43e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30007582.819004964 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0298254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0740293 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.42461e+08s, dt:163562s, Cycle: 942 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 4.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 5.31e-10 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-03 ) ; ( Rwell ) = ( 8.46e-14 ) ; ( R ) = ( 2.08e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.17e-06 ) ; ( Rwell ) = ( 3.60e-15 ) ; ( R ) = ( 9.17e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0714338 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.42625e+08s, dt:161359s, Cycle: 943 +well_1Control: BHP (at the specified reference elevation): 30016576.075197242 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.87e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 5.13e-10 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.05e-04 ) ; ( Rwell ) = ( 1.42e-13 ) ; ( R ) = ( 5.05e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0274174 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653042 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.42786e+08s, dt:168913s, Cycle: 944 +well_1Control: BHP (at the specified reference elevation): 30025444.324814238 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 7.37e-09 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 1.92e-12 ) ; ( R ) = ( 7.02e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.029155 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696355 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.42955e+08s, dt:45052.3s, Cycle: 945 +well_1Control: BHP (at the specified reference elevation): 30034710.054212175 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 1.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.32e-03 ) ; ( Rwell ) = ( 3.93e-11 ) ; ( R ) = ( 3.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-05 ) ; ( Rwell ) = ( 2.26e-14 ) ; ( R ) = ( 1.27e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00832169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0191033 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43e+08s, dt:87434.4s, Cycle: 946 +well_1Control: BHP (at the specified reference elevation): 30037186.59746431 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; ( R ) = ( 2.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 1.47e-10 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.98e-03 ) ; ( Rwell ) = ( 5.37e-14 ) ; ( R ) = ( 3.98e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e-05 ) ; ( Rwell ) = ( 6.58e-15 ) ; ( R ) = ( 1.84e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30041987.84031979 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0151172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0375583 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.73789e+07, 1.74181e+07, 1.74569e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.87635e+06, 4.95437e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.309 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.10022, 725.209 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3051.16, 702719 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 501.38, 212900 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2549.78, 489820 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.246, 0.477241 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2900.91, 702719 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3051.16, 0 }, { 947.502, 701752 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.73328e+07, 1.73647e+07, 1.73975e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.83029e+06, 4.89502e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.733 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.20492, 223.529 } rm^3 +compflowStatistics, caprock: Phase mass: { 87.9836, 216556 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 52.5912, 65026.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 35.3924, 151529 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8784, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 77.1052, 216556 } kg +compflowStatistics, caprock: Dissolved component mass: { { 87.9836, 0 }, { 144.035, 216409 } } kg +compflowStatistics: Max phase CFL number: 25.8712 +compflowStatistics: Max component CFL number: 35.3734 +Time: 1.43087e+08s, dt:126527s, Cycle: 947 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 3.86e-08 ) ; ( R ) = ( 3.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 3.05e-10 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 3.61e-14 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.31e-06 ) ; ( Rwell ) = ( 5.64e-15 ) ; ( R ) = ( 6.31e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0221057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0521499 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43214e+08s, dt:152443s, Cycle: 948 +well_1Control: BHP (at the specified reference elevation): 30048929.43149934 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 3.85e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.54e-05 ) ; ( Rwell ) = ( 6.00e-14 ) ; ( R ) = ( 6.54e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0256479 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643018 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43366e+08s, dt:161190s, Cycle: 949 +well_1Control: BHP (at the specified reference elevation): 30057272.491834633 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.84e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 4.84e-10 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 1.93e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.02e-03 ) ; ( Rwell ) = ( 1.26e-10 ) ; ( R ) = ( 9.02e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.96e-05 ) ; ( Rwell ) = ( 2.38e-14 ) ; ( R ) = ( 1.96e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0271438 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706958 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.43528e+08s, dt:160129s, Cycle: 950 +well_1Control: BHP (at the specified reference elevation): 30066088.079497583 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 4.85e-10 ) ; ( R ) = ( 2.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-04 ) ; ( Rwell ) = ( 6.97e-14 ) ; ( R ) = ( 3.50e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.027526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697349 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43688e+08s, dt:160534s, Cycle: 951 +well_1Control: BHP (at the specified reference elevation): 30074839.442914866 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 3.83e-08 ) ; ( R ) = ( 4.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 4.79e-10 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.56e-03 ) ; ( Rwell ) = ( 1.46e-13 ) ; ( R ) = ( 5.56e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-05 ) ; ( Rwell ) = ( 1.47e-15 ) ; ( R ) = ( 2.06e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0270335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654802 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.43848e+08s, dt:151742s, Cycle: 952 +well_1Control: BHP (at the specified reference elevation): 30083599.937271044 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 4.28e-10 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 1.07e-10 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.46e-05 ) ; ( Rwell ) = ( 1.68e-14 ) ; ( R ) = ( 8.46e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0257402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632504 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.44e+08s, dt:162166s, Cycle: 953 +well_1Control: BHP (at the specified reference elevation): 30091881.44773709 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.82e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 4.89e-10 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-04 ) ; ( Rwell ) = ( 6.12e-14 ) ; ( R ) = ( 2.39e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0271513 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624164 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.74094e+07, 1.74487e+07, 1.74875e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.90484e+06, 4.98286e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.332 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.14162, 725.19 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3075.86, 702718 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 503.242, 212911 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2572.62, 489806 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.866, 0.477256 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2924, 702717 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3075.86, 0 }, { 950.179, 701748 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.73635e+07, 1.73953e+07, 1.74281e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.85883e+06, 4.9235e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.74 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.210909, 223.529 } rm^3 +compflowStatistics, caprock: Phase mass: { 90.7599, 216562 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 53.6362, 65030.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 37.1237, 151531 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9454, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 79.8144, 216562 } kg +compflowStatistics, caprock: Dissolved component mass: { { 90.7599, 0 }, { 145.651, 216413 } } kg +well_1Control: BHP (at the specified reference elevation): 30100712.456966653 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 47.875 +compflowStatistics: Max component CFL number: 65.4625 +Time: 1.44162e+08s, dt:174790s, Cycle: 954 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.18e-02 ) ; ( Rwell ) = ( 5.65e-10 ) ; ( R ) = ( 9.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 1.92e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 2.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.18e-10 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 7.78e-11 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 7.21e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 1.08e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 1.26e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 1.35e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.43e-03 ) ; ( Rwell ) = ( 7.17e-11 ) ; ( R ) = ( 6.43e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.23e-04 ) ; ( Rwell ) = ( 9.88e-15 ) ; ( R ) = ( 7.23e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0298387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641714 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.44337e+08s, dt:185063s, Cycle: 955 +well_1Control: BHP (at the specified reference elevation): 30110226.173844505 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 6.38e-10 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.92e-04 ) ; ( Rwell ) = ( 2.05e-13 ) ; ( R ) = ( 7.92e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0307862 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701293 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.44522e+08s, dt:184835s, Cycle: 956 +well_1Control: BHP (at the specified reference elevation): 30120304.163393095 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 6.59e-09 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-03 ) ; ( Rwell ) = ( 1.26e-12 ) ; ( R ) = ( 2.54e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.19e-06 ) ; ( Rwell ) = ( 2.54e-15 ) ; ( R ) = ( 4.19e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0309923 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0700351 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.44707e+08s, dt:184774s, Cycle: 957 +well_1Control: BHP (at the specified reference elevation): 30130362.246259924 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 6.29e-10 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 2.55e-13 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.67e-06 ) ; ( Rwell ) = ( 1.26e-14 ) ; ( R ) = ( 1.67e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.54e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30140432.36000806 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0312415 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723099 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.44892e+08s, dt:108373s, Cycle: 958 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; ( R ) = ( 2.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.89e-03 ) ; ( Rwell ) = ( 2.20e-10 ) ; ( R ) = ( 9.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 7.00e-14 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.98e-06 ) ; ( Rwell ) = ( 5.25e-15 ) ; ( R ) = ( 5.98e-06 ) ; + Last LinSolve(iter,res) = ( 4, 9.74e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30146348.0999898 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0189856 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0427444 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45e+08s, dt:146366s, Cycle: 959 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 3.81e-08 ) ; ( R ) = ( 3.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 3.83e-10 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-04 ) ; ( Rwell ) = ( 1.21e-13 ) ; ( R ) = ( 1.03e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0244673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594362 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.74374e+07, 1.74766e+07, 1.75154e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.93322e+06, 5.01123e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.352 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.17933, 725.173 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3098.44, 702716 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 505.026, 212922 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2593.42, 489794 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 153.599, 0.47727 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2944.85, 702716 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3098.44, 0 }, { 952.661, 701744 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.73914e+07, 1.74233e+07, 1.7456e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.88729e+06, 4.95188e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.746 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.21645, 223.53 } rm^3 +compflowStatistics, caprock: Phase mass: { 93.3359, 216567 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 54.5947, 65033.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 38.7412, 151534 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9466, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 82.3893, 216567 } kg +compflowStatistics, caprock: Dissolved component mass: { { 93.3359, 0 }, { 147.111, 216417 } } kg +well_1Control: BHP (at the specified reference elevation): 30154321.103189513 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 43.1215 +compflowStatistics: Max component CFL number: 58.9656 +Time: 1.45146e+08s, dt:162739s, Cycle: 960 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.80e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 4.73e-10 ) ; ( R ) = ( 3.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 1.06e-13 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.84e-06 ) ; ( Rwell ) = ( 4.91e-16 ) ; ( R ) = ( 8.84e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.027122 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655885 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45309e+08s, dt:169876s, Cycle: 961 +well_1Control: BHP (at the specified reference elevation): 30163173.46419749 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 5.13e-10 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-03 ) ; ( Rwell ) = ( 4.27e-15 ) ; ( R ) = ( 1.14e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-06 ) ; ( Rwell ) = ( 1.02e-14 ) ; ( R ) = ( 3.67e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.028243 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641879 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45479e+08s, dt:179830s, Cycle: 962 +well_1Control: BHP (at the specified reference elevation): 30172410.416378103 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 5.76e-10 ) ; ( R ) = ( 5.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-02 ) ; ( Rwell ) = ( 1.46e-10 ) ; ( R ) = ( 1.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.59e-04 ) ; ( Rwell ) = ( 1.98e-14 ) ; ( R ) = ( 2.59e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0299117 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0591785 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.45659e+08s, dt:200493s, Cycle: 963 +well_1Control: BHP (at the specified reference elevation): 30182184.586778402 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 3.79e-08 ) ; ( R ) = ( 4.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 7.05e-10 ) ; ( R ) = ( 1.70e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.29e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 2.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 4.07e-10 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 2.33e-14 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.33e-06 ) ; ( Rwell ) = ( 7.99e-15 ) ; ( R ) = ( 2.33e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.66e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30193055.203908443 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0331838 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0740823 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.45859e+08s, dt:140696s, Cycle: 964 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; ( R ) = ( 3.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.50e-10 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 7.72e-14 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-06 ) ; ( Rwell ) = ( 1.76e-15 ) ; ( R ) = ( 1.85e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.05e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30200694.583174467 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0235904 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544719 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.46e+08s, dt:165115s, Cycle: 965 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 3.78e-08 ) ; ( R ) = ( 4.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 4.78e-10 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.67e-03 ) ; ( Rwell ) = ( 9.06e-14 ) ; ( R ) = ( 4.67e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 2.99e-15 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0275041 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612057 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.74662e+07, 1.75055e+07, 1.75443e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.96157e+06, 5.03958e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.373 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.21825, 725.155 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3121.81, 702715 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 506.855, 212933 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2614.96, 489782 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 155.198, 0.477284 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2966.62, 702714 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3121.81, 0 }, { 955.212, 701740 } } kg +well_1Control: BHP (at the specified reference elevation): 30209646.872786745 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, caprock: Pressure (min, average, max): 1.74204e+07, 1.74522e+07, 1.74849e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.91569e+06, 4.98023e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.753 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.222234, 223.531 } rm^3 +compflowStatistics, caprock: Phase mass: { 96.0328, 216573 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 55.5803, 65037.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 40.4525, 151536 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.843, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 85.1898, 216573 } kg +compflowStatistics, caprock: Dissolved component mass: { { 96.0328, 0 }, { 148.615, 216421 } } kg +compflowStatistics: Max phase CFL number: 48.5419 +compflowStatistics: Max component CFL number: 66.381 +Time: 1.46165e+08s, dt:180208s, Cycle: 966 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 5.68e-10 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.46e-10 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-03 ) ; ( Rwell ) = ( 2.65e-14 ) ; ( R ) = ( 1.02e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.60e-07 ) ; ( Rwell ) = ( 5.96e-16 ) ; ( R ) = ( 6.60e-07 ) ; + Last LinSolve(iter,res) = ( 8, 9.10e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0298111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753518 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.46345e+08s, dt:171468s, Cycle: 967 +well_1Control: BHP (at the specified reference elevation): 30219410.352499075 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 8.51e-09 ) ; ( R ) = ( 4.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.37e-03 ) ; ( Rwell ) = ( 5.78e-12 ) ; ( R ) = ( 5.37e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.08e-06 ) ; ( Rwell ) = ( 6.74e-15 ) ; ( R ) = ( 8.08e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0750204 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.46517e+08s, dt:163644s, Cycle: 968 +well_1Control: BHP (at the specified reference elevation): 30228706.94078857 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.68e-10 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.88e-04 ) ; ( Rwell ) = ( 1.15e-13 ) ; ( R ) = ( 9.88e-04 ) ; + Last LinSolve(iter,res) = ( 8, 4.52e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30237584.722923707 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0278591 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701239 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.4668e+08s, dt:163451s, Cycle: 969 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.77e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 4.66e-10 ) ; ( R ) = ( 2.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.94e-03 ) ; ( Rwell ) = ( 1.23e-13 ) ; ( R ) = ( 4.94e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.40e-05 ) ; ( Rwell ) = ( 1.23e-14 ) ; ( R ) = ( 1.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0276091 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.063697 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.46844e+08s, dt:156114s, Cycle: 970 +well_1Control: BHP (at the specified reference elevation): 30246434.43037322 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 3.76e-08 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 4.10e-10 ) ; ( R ) = ( 3.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.53e-03 ) ; ( Rwell ) = ( 1.52e-14 ) ; ( R ) = ( 3.53e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.80e-05 ) ; ( Rwell ) = ( 5.82e-16 ) ; ( R ) = ( 1.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0262259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0545774 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47e+08s, dt:182992s, Cycle: 971 +well_1Control: BHP (at the specified reference elevation): 30254874.53770534 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.08e-02 ) ; ( Rwell ) = ( 5.61e-10 ) ; ( R ) = ( 7.08e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 1.39e-10 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.22e-02 ) ; ( Rwell ) = ( 9.48e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 3.67e-11 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-05 ) ; ( Rwell ) = ( 3.35e-16 ) ; ( R ) = ( 1.19e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0301676 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0741654 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7495e+07, 1.75343e+07, 1.7573e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 4.98984e+06, 5.06786e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.394 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.25697, 725.137 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3145.14, 702713 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 508.677, 212944 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2636.46, 489769 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 156.715, 0.477298 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2988.42, 702713 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3145.14, 0 }, { 957.767, 701736 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74492e+07, 1.7481e+07, 1.75137e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.94403e+06, 5.0085e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.759 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.228063, 223.531 } rm^3 +compflowStatistics, caprock: Phase mass: { 98.7591, 216578 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 56.5633, 65040.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 42.1958, 151538 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8796, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 87.8795, 216578 } kg +compflowStatistics, caprock: Dissolved component mass: { { 98.7591, 0 }, { 150.105, 216425 } } kg +well_1Control: BHP (at the specified reference elevation): 30264756.409127608 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 53.6843 +compflowStatistics: Max component CFL number: 73.417 +Time: 1.47183e+08s, dt:176010s, Cycle: 972 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 5.17e-10 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 1.89e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.93e-03 ) ; ( Rwell ) = ( 1.34e-10 ) ; ( R ) = ( 8.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 2.20e-14 ) ; ( R ) = ( 5.78e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295384 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755585 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.47359e+08s, dt:167161s, Cycle: 973 +well_1Control: BHP (at the specified reference elevation): 30274260.621621408 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 4.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 4.69e-10 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 2.08e-13 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e-05 ) ; ( Rwell ) = ( 1.62e-14 ) ; ( R ) = ( 1.08e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0276949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0708855 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.47526e+08s, dt:165763s, Cycle: 974 +well_1Control: BHP (at the specified reference elevation): 30283293.90000669 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 4.59e-10 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.02e-03 ) ; ( Rwell ) = ( 2.17e-13 ) ; ( R ) = ( 6.02e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.86e-05 ) ; ( Rwell ) = ( 7.70e-15 ) ; ( R ) = ( 3.86e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0274033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648905 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47692e+08s, dt:174242s, Cycle: 975 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 3.75e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 5.08e-10 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30292258.003481373 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 2.31e-13 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-06 ) ; ( Rwell ) = ( 5.41e-15 ) ; ( R ) = ( 1.56e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0288555 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691841 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47866e+08s, dt:133833s, Cycle: 976 +well_1Control: BHP (at the specified reference elevation): 30301669.492490746 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 3.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 3.00e-10 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 1.23e-13 ) ; ( R ) = ( 8.47e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0221571 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0538255 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48e+08s, dt:158203s, Cycle: 977 +well_1Control: BHP (at the specified reference elevation): 30308904.439089507 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.74e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 1.34e-09 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.18e-05 ) ; ( Rwell ) = ( 1.76e-13 ) ; ( R ) = ( 8.18e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.026125 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0634739 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75225e+07, 1.75618e+07, 1.76005e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.01806e+06, 5.09608e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.414 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.29397, 725.12 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3167.49, 702712 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 510.437, 212954 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2657.05, 489757 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 158.298, 0.477312 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3009.19, 702711 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3167.49, 0 }, { 960.191, 701732 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74768e+07, 1.75085e+07, 1.75412e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.9723e+06, 5.03672e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.765 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.233695, 223.532 } rm^3 +compflowStatistics, caprock: Phase mass: { 101.401, 216584 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 57.5048, 65043.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 43.896, 151540 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9345, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 90.4663, 216584 } kg +compflowStatistics, caprock: Dissolved component mass: { { 101.401, 0 }, { 151.522, 216429 } } kg +well_1Control: BHP (at the specified reference elevation): 30317441.638074253 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 46.3187 +compflowStatistics: Max component CFL number: 63.347 +Time: 1.48158e+08s, dt:168688s, Cycle: 978 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.55e-02 ) ; ( Rwell ) = ( 4.69e-10 ) ; ( R ) = ( 2.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.19e-04 ) ; ( Rwell ) = ( 1.68e-13 ) ; ( R ) = ( 4.19e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0279387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664059 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48327e+08s, dt:174667s, Cycle: 979 +well_1Control: BHP (at the specified reference elevation): 30326527.19029955 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 5.03e-10 ) ; ( R ) = ( 7.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 1.33e-10 ) ; ( R ) = ( 1.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-05 ) ; ( Rwell ) = ( 1.31e-14 ) ; ( R ) = ( 5.72e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.43e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30335941.855626255 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0298229 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06117 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48502e+08s, dt:190704s, Cycle: 980 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.46e-02 ) ; ( Rwell ) = ( 5.89e-10 ) ; ( R ) = ( 9.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 1.88e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.80e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 3.31e-10 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.18e-03 ) ; ( Rwell ) = ( 5.97e-14 ) ; ( R ) = ( 3.18e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.81e-06 ) ; ( Rwell ) = ( 2.48e-15 ) ; ( R ) = ( 6.81e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0321938 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691458 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48692e+08s, dt:192268s, Cycle: 981 +well_1Control: BHP (at the specified reference elevation): 30346195.696142606 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.71e-02 ) ; ( Rwell ) = ( 5.87e-10 ) ; ( R ) = ( 9.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.36e-10 ) ; ( R ) = ( 3.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.29e-03 ) ; ( Rwell ) = ( 8.64e-11 ) ; ( R ) = ( 5.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.36e-05 ) ; ( Rwell ) = ( 1.86e-14 ) ; ( R ) = ( 2.36e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0314414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0748896 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.48885e+08s, dt:115471s, Cycle: 982 +well_1Control: BHP (at the specified reference elevation): 30356529.764838144 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 2.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 2.14e-10 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 8.82e-14 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-06 ) ; ( Rwell ) = ( 5.79e-15 ) ; ( R ) = ( 2.98e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0192797 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.045009 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49e+08s, dt:151538s, Cycle: 983 +well_1Control: BHP (at the specified reference elevation): 30362743.726952955 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 3.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 3.67e-10 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 7.56e-14 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.67e-06 ) ; ( Rwell ) = ( 5.39e-15 ) ; ( R ) = ( 4.67e-06 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0249575 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0503241 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75505e+07, 1.75897e+07, 1.76285e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04621e+06, 5.12422e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.434 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.33147, 725.103 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3190.21, 702710 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 512.225, 212965 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2677.99, 489745 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 159.842, 0.477326 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3030.37, 702710 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3190.21, 0 }, { 962.683, 701728 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75048e+07, 1.75365e+07, 1.75691e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00052e+06, 5.06486e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.239473, 223.532 } rm^3 +compflowStatistics, caprock: Phase mass: { 104.119, 216589 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 58.4597, 65047 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 45.659, 151542 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9433, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 93.1754, 216589 } kg +compflowStatistics, caprock: Dissolved component mass: { { 104.119, 0 }, { 152.958, 216433 } } kg +well_1Control: BHP (at the specified reference elevation): 30370898.4437846 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 44.2772 +compflowStatistics: Max component CFL number: 60.5578 +Time: 1.49152e+08s, dt:186483s, Cycle: 984 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 5.67e-10 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.25e-04 ) ; ( Rwell ) = ( 3.64e-14 ) ; ( R ) = ( 7.25e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0311437 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.055902 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49338e+08s, dt:215405s, Cycle: 985 +well_1Control: BHP (at the specified reference elevation): 30380925.078781664 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 3.71e-08 ) ; ( R ) = ( 4.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.04e-02 ) ; ( Rwell ) = ( 7.49e-10 ) ; ( R ) = ( 8.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 1.90e-10 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 2.90e-14 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0356083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657803 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49553e+08s, dt:224424s, Cycle: 986 +well_1Control: BHP (at the specified reference elevation): 30392499.880174078 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 8.02e-10 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.06e-10 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 9.41e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.59e-03 ) ; ( Rwell ) = ( 1.15e-10 ) ; ( R ) = ( 4.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 1.08e-14 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0368293 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0808646 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.49778e+08s, dt:203380s, Cycle: 987 +well_1Control: BHP (at the specified reference elevation): 30404554.43268794 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 4.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 3.54e-09 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 1.87e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 3.08e-09 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 2.88e-13 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0339342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701419 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.49981e+08s, dt:18769.9s, Cycle: 988 +well_1Control: BHP (at the specified reference elevation): 30415479.346556485 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 3.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-03 ) ; ( Rwell ) = ( 5.16e-12 ) ; ( R ) = ( 1.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-05 ) ; ( Rwell ) = ( 7.82e-15 ) ; ( R ) = ( 2.11e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00375395 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00640298 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.5e+08s, dt:37539.9s, Cycle: 989 +well_1Control: BHP (at the specified reference elevation): 30416489.182590287 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.86e-03 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 7.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.32e-03 ) ; ( Rwell ) = ( 2.18e-11 ) ; ( R ) = ( 2.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.04e-05 ) ; ( Rwell ) = ( 5.98e-15 ) ; ( R ) = ( 3.04e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.87e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30418508.12323107 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00660208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0124697 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75754e+07, 1.76146e+07, 1.76534e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07432e+06, 5.15233e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.452 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.36486, 725.087 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3210.5, 702709 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 513.856, 212975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2696.64, 489735 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 161.214, 0.477338 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3049.28, 702709 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3210.5, 0 }, { 964.878, 701725 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75297e+07, 1.75614e+07, 1.7594e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02867e+06, 5.09298e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.244667, 223.532 } rm^3 +compflowStatistics, caprock: Phase mass: { 106.569, 216594 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 59.3077, 65049.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 47.2609, 151544 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8473, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 95.7213, 216594 } kg +compflowStatistics, caprock: Dissolved component mass: { { 106.569, 0 }, { 154.228, 216436 } } kg +compflowStatistics: Max phase CFL number: 10.9488 +compflowStatistics: Max component CFL number: 14.9753 +Time: 1.50038e+08s, dt:75079.7s, Cycle: 990 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 1.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.11e-03 ) ; ( Rwell ) = ( 8.73e-11 ) ; ( R ) = ( 8.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-04 ) ; ( Rwell ) = ( 1.02e-13 ) ; ( R ) = ( 2.24e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0125489 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.024063 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50113e+08s, dt:133474s, Cycle: 991 +well_1Control: BHP (at the specified reference elevation): 30422540.712297373 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 3.70e-08 ) ; ( R ) = ( 2.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 2.78e-10 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 1.75e-13 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0223526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.045182 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50246e+08s, dt:174787s, Cycle: 992 +well_1Control: BHP (at the specified reference elevation): 30429697.607579228 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 3.69e-08 ) ; ( R ) = ( 3.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 4.77e-10 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 1.86e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.16e-10 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e-04 ) ; ( Rwell ) = ( 5.59e-14 ) ; ( R ) = ( 1.73e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0284764 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613829 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50421e+08s, dt:190414s, Cycle: 993 +well_1Control: BHP (at the specified reference elevation): 30439052.22197879 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 5.52e-10 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-03 ) ; ( Rwell ) = ( 7.51e-14 ) ; ( R ) = ( 2.16e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-06 ) ; ( Rwell ) = ( 1.68e-14 ) ; ( R ) = ( 2.71e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0309728 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681269 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50611e+08s, dt:193872s, Cycle: 994 +well_1Control: BHP (at the specified reference elevation): 30449247.75118963 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 5.73e-10 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-03 ) ; ( Rwell ) = ( 1.99e-13 ) ; ( R ) = ( 1.22e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.33e-06 ) ; ( Rwell ) = ( 1.66e-15 ) ; ( R ) = ( 2.33e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0318789 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681736 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.50805e+08s, dt:194834s, Cycle: 995 +well_1Control: BHP (at the specified reference elevation): 30459636.08700805 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 5.83e-10 ) ; ( R ) = ( 4.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 1.48e-10 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 1.53e-14 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e-05 ) ; ( Rwell ) = ( 2.36e-15 ) ; ( R ) = ( 1.34e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0322711 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06205 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.51e+08s, dt:210794s, Cycle: 996 +well_1Control: BHP (at the specified reference elevation): 30470073.835957438 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 6.67e-10 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 1.73e-10 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 9.31e-09 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.17e-03 ) ; ( Rwell ) = ( 4.29e-11 ) ; ( R ) = ( 6.17e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.91e-05 ) ; ( Rwell ) = ( 8.04e-15 ) ; ( R ) = ( 1.91e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0342544 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0699855 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76083e+07, 1.76475e+07, 1.76863e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10237e+06, 5.18039e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.476 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.40894, 725.067 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3237.35, 702708 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 515.919, 212987 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2721.43, 489721 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 162.919, 0.477353 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3074.43, 702707 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3237.35, 0 }, { 967.764, 701720 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75627e+07, 1.75943e+07, 1.76269e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05678e+06, 5.12103e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.251595, 223.533 } rm^3 +compflowStatistics, caprock: Phase mass: { 109.846, 216600 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 60.4244, 65053.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 49.4216, 151546 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8584, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 98.9875, 216600 } kg +compflowStatistics, caprock: Dissolved component mass: { { 109.846, 0 }, { 155.902, 216441 } } kg +well_1Control: BHP (at the specified reference elevation): 30481358.087142028 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 61.3334 +compflowStatistics: Max component CFL number: 83.8938 +Time: 1.51211e+08s, dt:210823s, Cycle: 997 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.08e-02 ) ; ( Rwell ) = ( 6.74e-10 ) ; ( R ) = ( 8.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 1.85e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 2.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 3.82e-10 ) ; ( R ) = ( 5.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 1.39e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.58e-03 ) ; ( Rwell ) = ( 9.82e-11 ) ; ( R ) = ( 5.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.91e-05 ) ; ( Rwell ) = ( 2.18e-14 ) ; ( R ) = ( 5.91e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0343996 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0959314 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.51422e+08s, dt:169069s, Cycle: 998 +well_1Control: BHP (at the specified reference elevation): 30492649.83395382 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 4.37e-10 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-04 ) ; ( Rwell ) = ( 3.17e-13 ) ; ( R ) = ( 2.20e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0285922 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0815458 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.51591e+08s, dt:152320s, Cycle: 999 +well_1Control: BHP (at the specified reference elevation): 30501717.372714877 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 3.68e-08 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 2.15e-09 ) ; ( R ) = ( 7.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-04 ) ; ( Rwell ) = ( 1.94e-13 ) ; ( R ) = ( 1.33e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0249549 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716704 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.51743e+08s, dt:149934s, Cycle: 1000 +well_1Control: BHP (at the specified reference elevation): 30509879.20580899 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.37e-10 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.16e-04 ) ; ( Rwell ) = ( 3.23e-13 ) ; ( R ) = ( 4.16e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0246401 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638326 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.51893e+08s, dt:107061s, Cycle: 1001 +well_1Control: BHP (at the specified reference elevation): 30517913.829332974 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 3.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.04e-03 ) ; ( Rwell ) = ( 1.74e-10 ) ; ( R ) = ( 7.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.01e-04 ) ; ( Rwell ) = ( 1.07e-13 ) ; ( R ) = ( 5.01e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.81e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30523653.32318239 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0175749 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0431586 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52e+08s, dt:143829s, Cycle: 1002 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 3.67e-08 ) ; ( R ) = ( 3.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 3.09e-10 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 1.84e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.41e-03 ) ; ( Rwell ) = ( 7.22e-11 ) ; ( R ) = ( 9.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-05 ) ; ( Rwell ) = ( 4.26e-14 ) ; ( R ) = ( 2.51e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0233336 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0548671 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76345e+07, 1.76737e+07, 1.77125e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13044e+06, 5.20845e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.495 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.44407, 725.051 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3258.79, 702707 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 517.628, 212997 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2741.16, 489709 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 164.195, 0.477366 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3094.6, 702706 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3258.79, 0 }, { 969.943, 701717 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75889e+07, 1.76205e+07, 1.76531e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08485e+06, 5.14909e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.257146, 223.533 } rm^3 +compflowStatistics, caprock: Phase mass: { 112.48, 216605 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 61.3081, 65056.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 51.1724, 151548 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8444, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 101.636, 216605 } kg +compflowStatistics, caprock: Dissolved component mass: { { 112.48, 0 }, { 157.232, 216444 } } kg +well_1Control: BHP (at the specified reference elevation): 30531347.45601119 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 41.7701 +compflowStatistics: Max component CFL number: 57.137 +Time: 1.52144e+08s, dt:168048s, Cycle: 1003 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 4.08e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 1.96e-13 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-05 ) ; ( Rwell ) = ( 2.86e-15 ) ; ( R ) = ( 2.23e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0274222 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636163 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52312e+08s, dt:178926s, Cycle: 1004 +well_1Control: BHP (at the specified reference elevation): 30540323.20670822 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 3.65e-08 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 4.65e-10 ) ; ( R ) = ( 3.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.15e-03 ) ; ( Rwell ) = ( 1.48e-14 ) ; ( R ) = ( 4.15e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.19e-06 ) ; ( Rwell ) = ( 2.40e-15 ) ; ( R ) = ( 9.19e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0290984 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633397 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52491e+08s, dt:191045s, Cycle: 1005 +well_1Control: BHP (at the specified reference elevation): 30549867.43890205 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 5.30e-10 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 6.10e-14 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-06 ) ; ( Rwell ) = ( 2.55e-15 ) ; ( R ) = ( 1.46e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0308651 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600533 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52682e+08s, dt:211036s, Cycle: 1006 +well_1Control: BHP (at the specified reference elevation): 30560038.34791354 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 6.29e-10 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.52e-03 ) ; ( Rwell ) = ( 3.64e-13 ) ; ( R ) = ( 2.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-05 ) ; ( Rwell ) = ( 4.11e-15 ) ; ( R ) = ( 2.06e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0344153 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602079 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52893e+08s, dt:107116s, Cycle: 1007 +well_1Control: BHP (at the specified reference elevation): 30571266.962005652 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 2.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 1.63e-10 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.34e-04 ) ; ( Rwell ) = ( 2.18e-14 ) ; ( R ) = ( 4.34e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0176308 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.033738 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.53e+08s, dt:163624s, Cycle: 1008 +well_1Control: BHP (at the specified reference elevation): 30576970.714871503 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 2.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 3.83e-10 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 5.47e-14 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-05 ) ; ( Rwell ) = ( 8.20e-15 ) ; ( R ) = ( 1.05e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0264065 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0465406 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7663e+07, 1.77022e+07, 1.7741e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1584e+06, 5.23641e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.516 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.48217, 725.034 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3282.13, 702705 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 519.332, 213008 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2762.79, 489697 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 165.618, 0.47738 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3116.51, 702705 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3282.13, 0 }, { 972.406, 701713 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76175e+07, 1.7649e+07, 1.76816e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11289e+06, 5.17706e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.797 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.26324, 223.533 } rm^3 +compflowStatistics, caprock: Phase mass: { 115.381, 216610 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 62.2648, 65060.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 53.1164, 151550 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.7908, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 104.59, 216610 } kg +compflowStatistics, caprock: Dissolved component mass: { { 115.381, 0 }, { 158.686, 216448 } } kg +well_1Control: BHP (at the specified reference elevation): 30585677.29440117 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 47.422 +compflowStatistics: Max component CFL number: 64.8713 +Time: 1.53164e+08s, dt:210699s, Cycle: 1009 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 6.22e-10 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 1.83e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 1.61e-10 ) ; ( R ) = ( 9.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 5.05e-15 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.035011 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658236 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.53374e+08s, dt:219427s, Cycle: 1010 +well_1Control: BHP (at the specified reference elevation): 30596860.869788308 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 4.61e-09 ) ; ( R ) = ( 3.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 2.57e-13 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.62e-06 ) ; ( Rwell ) = ( 8.59e-16 ) ; ( R ) = ( 9.62e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.035691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0807121 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.53594e+08s, dt:199113s, Cycle: 1011 +well_1Control: BHP (at the specified reference elevation): 30608499.431730777 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; ( R ) = ( 4.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.67e-02 ) ; ( Rwell ) = ( 5.52e-10 ) ; ( R ) = ( 9.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 1.82e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.71e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 3.17e-10 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 3.10e-14 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.02e-07 ) ; ( Rwell ) = ( 6.27e-16 ) ; ( R ) = ( 4.02e-07 ) ; + Last LinSolve(iter,res) = ( 8, 7.98e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0319607 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0788005 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.53793e+08s, dt:183716s, Cycle: 1012 +well_1Control: BHP (at the specified reference elevation): 30619051.524469297 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 4.71e-10 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 3.44e-13 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.03e-07 ) ; ( Rwell ) = ( 6.32e-15 ) ; ( R ) = ( 9.03e-07 ) ; + Last LinSolve(iter,res) = ( 7, 1.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0295087 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716792 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.53977e+08s, dt:23420.4s, Cycle: 1013 +well_1Control: BHP (at the specified reference elevation): 30628776.97613933 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-03 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 1.55e-11 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-05 ) ; ( Rwell ) = ( 1.87e-14 ) ; ( R ) = ( 1.03e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00428735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00915281 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.54e+08s, dt:46840.9s, Cycle: 1014 +well_1Control: BHP (at the specified reference elevation): 30630017.781849086 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 1.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-03 ) ; ( Rwell ) = ( 2.96e-11 ) ; ( R ) = ( 3.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-05 ) ; ( Rwell ) = ( 4.03e-14 ) ; ( R ) = ( 1.20e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00786432 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.018254 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76875e+07, 1.77268e+07, 1.77655e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18623e+06, 5.26424e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.534 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.51488, 725.019 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3302.23, 702704 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 520.783, 213017 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2781.45, 489687 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 166.906, 0.477392 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3135.32, 702704 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3302.23, 0 }, { 974.632, 701710 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76421e+07, 1.76736e+07, 1.77062e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14083e+06, 5.20489e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.802 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.268542, 223.534 } rm^3 +compflowStatistics, caprock: Phase mass: { 117.911, 216614 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 63.0867, 65063.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 54.8244, 151551 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.7721, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 107.139, 216614 } kg +compflowStatistics, caprock: Dissolved component mass: { { 117.911, 0 }, { 159.941, 216451 } } kg +well_1Control: BHP (at the specified reference elevation): 30632498.488441672 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 13.5517 +compflowStatistics: Max component CFL number: 18.5389 +Time: 1.54047e+08s, dt:92355.4s, Cycle: 1015 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.38e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 2.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.32e-03 ) ; ( Rwell ) = ( 1.12e-10 ) ; ( R ) = ( 9.32e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 9.98e-14 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 8, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.78e-06 ) ; ( Rwell ) = ( 7.35e-15 ) ; ( R ) = ( 9.78e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0159135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0363015 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54139e+08s, dt:136004s, Cycle: 1016 +well_1Control: BHP (at the specified reference elevation): 30637390.197830282 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 3.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 2.49e-10 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.42e-14 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.78e-06 ) ; ( Rwell ) = ( 8.65e-15 ) ; ( R ) = ( 2.78e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0220354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0552857 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54275e+08s, dt:158170s, Cycle: 1017 +well_1Control: BHP (at the specified reference elevation): 30644588.195631534 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 3.39e-10 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.77e-03 ) ; ( Rwell ) = ( 2.06e-13 ) ; ( R ) = ( 3.77e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 5.53e-15 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0253931 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0576734 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54433e+08s, dt:179208s, Cycle: 1018 +well_1Control: BHP (at the specified reference elevation): 30652960.590577617 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 4.38e-10 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.86e-03 ) ; ( Rwell ) = ( 1.12e-10 ) ; ( R ) = ( 6.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.00e-05 ) ; ( Rwell ) = ( 5.62e-14 ) ; ( R ) = ( 8.00e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0288589 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064595 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.54613e+08s, dt:188934s, Cycle: 1019 +well_1Control: BHP (at the specified reference elevation): 30662445.196806706 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 4.84e-10 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 1.26e-10 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 6.82e-14 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.030732 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0766714 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.54802e+08s, dt:177646s, Cycle: 1020 +well_1Control: BHP (at the specified reference elevation): 30672471.103757966 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 4.28e-10 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 1.09e-13 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.78e-04 ) ; ( Rwell ) = ( 1.90e-15 ) ; ( R ) = ( 3.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0291389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0745141 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.54979e+08s, dt:20841.7s, Cycle: 1021 +well_1Control: BHP (at the specified reference elevation): 30681900.06841182 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.55e-03 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 5.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 4.33e-12 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.15e-06 ) ; ( Rwell ) = ( 1.25e-15 ) ; ( R ) = ( 7.15e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00394117 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.00872387 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.55e+08s, dt:41683.5s, Cycle: 1022 +well_1Control: BHP (at the specified reference elevation): 30683007.660219483 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.61e-08 ) ; ( R ) = ( 1.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 2.27e-11 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 8.80e-15 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.95e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30685221.871029172 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00713259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0174411 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77152e+07, 1.77545e+07, 1.77932e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21406e+06, 5.29207e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.554 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.5518, 725.002 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3324.96, 702703 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 522.609, 213028 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2802.35, 489675 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 168.417, 0.477406 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3156.54, 702703 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3324.96, 0 }, { 977.027, 701706 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76698e+07, 1.77013e+07, 1.77339e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16869e+06, 5.23272e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.808 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.274549, 223.534 } rm^3 +compflowStatistics, caprock: Phase mass: { 120.786, 216619 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 64.005, 65066.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 56.7806, 151553 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.6231, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 110.163, 216619 } kg +compflowStatistics, caprock: Dissolved component mass: { { 120.786, 0 }, { 161.353, 216455 } } kg +compflowStatistics: Max phase CFL number: 12.0358 +compflowStatistics: Max component CFL number: 16.4659 +Time: 1.55042e+08s, dt:83367s, Cycle: 1023 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 2.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.42e-03 ) ; ( Rwell ) = ( 9.65e-11 ) ; ( R ) = ( 8.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.08e-04 ) ; ( Rwell ) = ( 7.14e-14 ) ; ( R ) = ( 7.08e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0136522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0344474 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55125e+08s, dt:126046s, Cycle: 1024 +well_1Control: BHP (at the specified reference elevation): 30689646.117849566 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 3.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 2.16e-10 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.09e-05 ) ; ( Rwell ) = ( 1.14e-13 ) ; ( R ) = ( 9.09e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0205052 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0495351 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55251e+08s, dt:156560s, Cycle: 1025 +well_1Control: BHP (at the specified reference elevation): 30696332.626628056 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.60e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 4.45e-09 ) ; ( R ) = ( 3.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.88e-04 ) ; ( Rwell ) = ( 1.03e-13 ) ; ( R ) = ( 5.88e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0251792 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.058817 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55408e+08s, dt:175221s, Cycle: 1026 +well_1Control: BHP (at the specified reference elevation): 30704629.970867418 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 4.07e-10 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 3.72e-13 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-06 ) ; ( Rwell ) = ( 1.22e-14 ) ; ( R ) = ( 1.43e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.028467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663632 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55583e+08s, dt:181508s, Cycle: 1027 +well_1Control: BHP (at the specified reference elevation): 30713908.790463928 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.59e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 4.41e-10 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 2.69e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 2.53e-10 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 7.61e-14 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.29e-07 ) ; ( Rwell ) = ( 8.10e-15 ) ; ( R ) = ( 5.29e-07 ) ; + Last LinSolve(iter,res) = ( 6, 1.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0291757 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601772 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55764e+08s, dt:200241s, Cycle: 1028 +well_1Control: BHP (at the specified reference elevation): 30723505.584710628 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 3.58e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 5.27e-10 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 2.84e-14 ) ; ( R ) = ( 5.83e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0319136 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.062759 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55965e+08s, dt:35373.9s, Cycle: 1029 +well_1Control: BHP (at the specified reference elevation): 30734076.80805718 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-03 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-03 ) ; ( Rwell ) = ( 1.33e-11 ) ; ( R ) = ( 2.43e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.06e-05 ) ; ( Rwell ) = ( 5.53e-16 ) ; ( R ) = ( 4.06e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.87e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30735946.67412017 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.00643786 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0115269 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1.56e+08s, dt:70747.8s, Cycle: 1030 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 1.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.87e-03 ) ; ( Rwell ) = ( 6.57e-11 ) ; ( R ) = ( 8.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.13e-05 ) ; ( Rwell ) = ( 3.77e-14 ) ; ( R ) = ( 3.13e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.94e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0115652 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0241804 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77438e+07, 1.77831e+07, 1.78219e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24188e+06, 5.31989e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.575 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.58998, 724.985 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3348.53, 702702 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 524.42, 213039 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2824.11, 489663 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 169.74, 0.47742 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3178.79, 702702 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3348.53, 0 }, { 979.427, 701703 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76985e+07, 1.77299e+07, 1.77625e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19653e+06, 5.26054e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.815 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.280802, 223.534 } rm^3 +compflowStatistics, caprock: Phase mass: { 123.787, 216624 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 64.9527, 65069.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 58.8343, 151555 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.7348, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 113.052, 216624 } kg +compflowStatistics, caprock: Dissolved component mass: { { 123.787, 0 }, { 162.813, 216458 } } kg +well_1Control: BHP (at the specified reference elevation): 30739685.39556916 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 20.3865 +compflowStatistics: Max component CFL number: 27.8916 +Time: 1.56071e+08s, dt:125523s, Cycle: 1031 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 2.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.04e-02 ) ; ( Rwell ) = ( 2.06e-10 ) ; ( R ) = ( 1.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 7.04e-14 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 8, 6.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0202272 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0448732 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56196e+08s, dt:165011s, Cycle: 1032 +well_1Control: BHP (at the specified reference elevation): 30746315.206671067 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 3.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 3.48e-10 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.44e-04 ) ; ( Rwell ) = ( 1.92e-13 ) ; ( R ) = ( 9.44e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0264453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0592246 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56361e+08s, dt:183881s, Cycle: 1033 +well_1Control: BHP (at the specified reference elevation): 30755030.06139291 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 4.38e-10 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.90e-04 ) ; ( Rwell ) = ( 1.15e-14 ) ; ( R ) = ( 5.90e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.030038 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649474 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56545e+08s, dt:193177s, Cycle: 1034 +well_1Control: BHP (at the specified reference elevation): 30764728.639276534 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 4.83e-10 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.88e-03 ) ; ( Rwell ) = ( 6.84e-15 ) ; ( R ) = ( 8.88e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 1.09e-14 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0307947 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730456 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.56738e+08s, dt:187732s, Cycle: 1035 +well_1Control: BHP (at the specified reference elevation): 30774911.63293568 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; ( R ) = ( 4.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.46e-10 ) ; ( R ) = ( 4.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.74e-03 ) ; ( Rwell ) = ( 1.02e-13 ) ; ( R ) = ( 7.74e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 3.21e-15 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0298269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701346 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.56926e+08s, dt:73927.1s, Cycle: 1036 +well_1Control: BHP (at the specified reference elevation): 30784791.913334675 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.84e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; ( R ) = ( 1.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-03 ) ; ( Rwell ) = ( 7.18e-11 ) ; ( R ) = ( 4.27e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.99e-05 ) ; ( Rwell ) = ( 1.39e-15 ) ; ( R ) = ( 2.99e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0263725 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57e+08s, dt:126479s, Cycle: 1037 +well_1Control: BHP (at the specified reference elevation): 30788687.89333532 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; ( R ) = ( 3.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.88e-03 ) ; ( Rwell ) = ( 1.41e-09 ) ; ( R ) = ( 9.88e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.28e-04 ) ; ( Rwell ) = ( 4.93e-13 ) ; ( R ) = ( 4.28e-04 ) ; + Last LinSolve(iter,res) = ( 8, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0208477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0423604 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: BHP (at the specified reference elevation): 30795351.289130025 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics, reservoir: Pressure (min, average, max): 1.77731e+07, 1.78124e+07, 1.78511e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26962e+06, 5.34764e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.596 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.62896, 724.967 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3372.65, 702701 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 526.2, 213050 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2846.45, 489651 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 171.069, 0.477434 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3201.58, 702701 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3372.65, 0 }, { 981.925, 701699 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77278e+07, 1.77592e+07, 1.77918e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22434e+06, 5.28828e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.821 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.287254, 223.534 } rm^3 +compflowStatistics, caprock: Phase mass: { 126.893, 216630 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 65.9197, 65073.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 60.973, 151556 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.6721, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 116.221, 216630 } kg +compflowStatistics, caprock: Dissolved component mass: { { 126.893, 0 }, { 164.303, 216462 } } kg +compflowStatistics: Max phase CFL number: 36.3704 +compflowStatistics: Max component CFL number: 49.7621 +Time: 1.57126e+08s, dt:171668s, Cycle: 1038 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; ( R ) = ( 3.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 3.70e-10 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e-03 ) ; ( Rwell ) = ( 5.52e-14 ) ; ( R ) = ( 1.10e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-07 ) ; ( Rwell ) = ( 2.88e-15 ) ; ( R ) = ( 2.99e-07 ) ; + Last LinSolve(iter,res) = ( 8, 5.15e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0272775 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06032 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57298e+08s, dt:189101s, Cycle: 1039 +well_1Control: BHP (at the specified reference elevation): 30804381.512024492 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 4.49e-10 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-03 ) ; ( Rwell ) = ( 1.04e-13 ) ; ( R ) = ( 2.34e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.23e-06 ) ; ( Rwell ) = ( 6.14e-15 ) ; ( R ) = ( 6.23e-06 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0302486 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665412 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57487e+08s, dt:195543s, Cycle: 1040 +well_1Control: BHP (at the specified reference elevation): 30814339.94788891 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 3.55e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 4.66e-10 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 1.20e-10 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 8.96e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.34e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.36e-03 ) ; ( Rwell ) = ( 6.80e-11 ) ; ( R ) = ( 9.36e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.15e-04 ) ; ( Rwell ) = ( 5.06e-14 ) ; ( R ) = ( 1.15e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.68e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30824613.457512032 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0316528 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653219 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57683e+08s, dt:204661s, Cycle: 1041 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 5.07e-10 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.78e-03 ) ; ( Rwell ) = ( 1.31e-10 ) ; ( R ) = ( 7.78e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.25e-05 ) ; ( Rwell ) = ( 2.17e-14 ) ; ( R ) = ( 3.25e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.09e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 30835356.765423194 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0327655 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607871 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.57887e+08s, dt:112548s, Cycle: 1042 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.70e-03 ) ; ( Rwell ) = ( 1.50e-10 ) ; ( R ) = ( 7.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-05 ) ; ( Rwell ) = ( 9.30e-14 ) ; ( R ) = ( 3.26e-05 ) ; + Last LinSolve(iter,res) = ( 8, 4.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0181056 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.032849 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.58e+08s, dt:174174s, Cycle: 1043 +well_1Control: BHP (at the specified reference elevation): 30841262.33943713 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; ( R ) = ( 3.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 3.67e-10 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 8.48e-14 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.18e-05 ) ; ( Rwell ) = ( 6.83e-15 ) ; ( R ) = ( 4.18e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0278327 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0522931 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78021e+07, 1.78414e+07, 1.78801e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2973e+06, 5.37531e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.617 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.66748, 724.95 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3396.56, 702700 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 528.064, 213061 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2868.5, 489639 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 172.662, 0.477449 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3223.9, 702700 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3396.56, 0 }, { 984.404, 701696 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77569e+07, 1.77883e+07, 1.78208e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25207e+06, 5.31595e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.828 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.293685, 223.534 } rm^3 +compflowStatistics, caprock: Phase mass: { 129.998, 216635 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 66.8683, 65076.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 63.1298, 151558 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.4886, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 119.51, 216635 } kg +compflowStatistics, caprock: Dissolved component mass: { { 129.998, 0 }, { 165.783, 216465 } } kg +well_1Control: BHP (at the specified reference elevation): 30850398.88213591 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 49.9833 +compflowStatistics: Max component CFL number: 68.3906 +Time: 1.58174e+08s, dt:209504s, Cycle: 1044 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 5.31e-10 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 4.94e-13 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 7, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-05 ) ; ( Rwell ) = ( 4.36e-15 ) ; ( R ) = ( 1.51e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0332399 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621283 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.58384e+08s, dt:226483s, Cycle: 1045 +well_1Control: BHP (at the specified reference elevation): 30861395.460487045 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 3.53e-08 ) ; ( R ) = ( 3.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 6.22e-10 ) ; ( R ) = ( 4.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.00e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.61e-10 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.99e-04 ) ; ( Rwell ) = ( 9.98e-15 ) ; ( R ) = ( 7.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.15e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0357913 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0714419 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.5861e+08s, dt:223415s, Cycle: 1046 +well_1Control: BHP (at the specified reference elevation): 30873273.320371136 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.74e-02 ) ; ( Rwell ) = ( 6.05e-10 ) ; ( R ) = ( 6.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.36e-02 ) ; ( Rwell ) = ( 1.78e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 1.55e-10 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.97e-04 ) ; ( Rwell ) = ( 2.52e-14 ) ; ( R ) = ( 2.97e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0361982 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0776285 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.58834e+08s, dt:166424s, Cycle: 1047 +well_1Control: BHP (at the specified reference elevation): 30884987.97604432 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; ( R ) = ( 3.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-03 ) ; ( Rwell ) = ( 5.07e-13 ) ; ( R ) = ( 3.03e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.25e-06 ) ; ( Rwell ) = ( 1.34e-14 ) ; ( R ) = ( 7.25e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0270784 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602188 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59e+08s, dt:183520s, Cycle: 1048 +well_1Control: BHP (at the specified reference elevation): 30893723.020140745 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 4.04e-10 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.08e-03 ) ; ( Rwell ) = ( 1.08e-13 ) ; ( R ) = ( 4.08e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.53e-05 ) ; ( Rwell ) = ( 2.56e-15 ) ; ( R ) = ( 2.53e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0290958 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0712904 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.783e+07, 1.78693e+07, 1.7908e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.32493e+06, 5.40294e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.637 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.70454, 724.933 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3419.62, 702699 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 529.8, 213072 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2889.82, 489627 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 173.926, 0.613561 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3245.69, 702699 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3419.62, 0 }, { 986.747, 701692 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77848e+07, 1.78162e+07, 1.78487e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27975e+06, 5.34359e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.834 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.299911, 223.534 } rm^3 +compflowStatistics, caprock: Phase mass: { 133.013, 216639 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 67.7727, 65079.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 65.2405, 151560 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.4289, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 122.584, 216639 } kg +compflowStatistics, caprock: Dissolved component mass: { { 133.013, 0 }, { 167.21, 216469 } } kg +well_1Control: BHP (at the specified reference elevation): 30903348.047655955 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s +compflowStatistics: Max phase CFL number: 52.5622 +compflowStatistics: Max component CFL number: 71.9225 +Time: 1.59184e+08s, dt:181292s, Cycle: 1049 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 3.52e-08 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 3.87e-10 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 1.30e-13 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0286834 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0731915 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.59365e+08s, dt:175944s, Cycle: 1050 +well_1Control: BHP (at the specified reference elevation): 30912841.90116128 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.54e-10 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.63e-04 ) ; ( Rwell ) = ( 9.24e-14 ) ; ( R ) = ( 4.63e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0279173 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069985 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59541e+08s, dt:175969s, Cycle: 1051 +well_1Control: BHP (at the specified reference elevation): 30922044.820974216 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; ( R ) = ( 4.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 3.53e-10 ) ; ( R ) = ( 6.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.10e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 8.78e-11 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 8.82e-09 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.32e-08 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 1.54e-08 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 7.99e-11 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.63e-05 ) ; ( Rwell ) = ( 2.45e-14 ) ; ( R ) = ( 8.63e-05 ) ; + Last LinSolve(iter,res) = ( 8, 6.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.028405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650748 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59717e+08s, dt:184629s, Cycle: 1052 +well_1Control: BHP (at the specified reference elevation): 30931242.11990954 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 3.93e-10 ) ; ( R ) = ( 9.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 1.02e-10 ) ; ( R ) = ( 1.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 2.25e-15 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.95e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0291614 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675895 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59901e+08s, dt:98646.2s, Cycle: 1053 +well_1Control: BHP (at the specified reference elevation): 30940889.47262838 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 3.50e-08 ) ; ( R ) = ( 2.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.65e-03 ) ; ( Rwell ) = ( 1.12e-10 ) ; ( R ) = ( 7.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.28e-05 ) ; ( Rwell ) = ( 3.32e-14 ) ; ( R ) = ( 3.28e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0166354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0349849 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6e+08s, dt:1e+06s, Cycle: 1054 +well_1Control: BHP (at the specified reference elevation): 30946053.412385423 Pa +well_1Control: Total rate: 2.9566997749602503e-05 kg/s; total surface volumetric rate: 2e-06 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987315e-06 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855634e-18 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e+02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e+02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e+02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e+02 ) ; + Last LinSolve(iter,res) = ( 31, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e+02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e+02 ) ; + Last LinSolve(iter,res) = ( 29, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e+02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e+02 ) ; + Last LinSolve(iter,res) = ( 27, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e+02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+02 ) ; + Last LinSolve(iter,res) = ( 26, 7.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.21e+01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.21e+01 ) ; + Last LinSolve(iter,res) = ( 24, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.57e+01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.57e+01 ) ; + Last LinSolve(iter,res) = ( 22, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.72e+01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e+01 ) ; + Last LinSolve(iter,res) = ( 20, 7.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.84e+01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e+01 ) ; + Last LinSolve(iter,res) = ( 18, 9.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.40e+01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e+01 ) ; + Last LinSolve(iter,res) = ( 15, 9.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.13e-01 ) ; + Last LinSolve(iter,res) = ( 13, 8.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.50e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-04 ) ; + Last LinSolve(iter,res) = ( 12, 7.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.083171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.453746 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.78487e+07, 1.78877e+07, 1.79243e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.35253e+06, 5.43054e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.651 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.72259, 724.928 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3431.93, 702706 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 532.51, 213079 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2899.42, 489627 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 174.187, 0.410086 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3257.74, 702705 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3431.93, 0 }, { 992.755, 701693 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78206e+07, 1.7841e+07, 1.78673e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.30739e+06, 5.37118e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.839 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.308566, 223.531 } rm^3 +compflowStatistics, caprock: Phase mass: { 137.031, 216641 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 68.9281, 65082.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 68.103, 151558 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.3039, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 126.727, 216641 } kg +compflowStatistics, caprock: Dissolved component mass: { { 137.031, 0 }, { 169.018, 216468 } } kg +compflowStatistics: Max phase CFL number: 4.91992 +compflowStatistics: Max component CFL number: 4.43434 +Time: 1.61e+08s, dt:1e+06s, Cycle: 1055 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.98e-01 ) ; + Last LinSolve(iter,res) = ( 13, 8.32e-03 ) ; + Line search @ 0.115: ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-01 ) ; + Last LinSolve(iter,res) = ( 14, 7.49e-03 ) ; + Line search @ 0.147: ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.42e-03 ) ; + Line search @ 0.155: ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.39e-01 ) ; + Last LinSolve(iter,res) = ( 13, 6.80e-03 ) ; + Line search @ 0.191: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-01 ) ; + Last LinSolve(iter,res) = ( 13, 6.97e-03 ) ; + Line search @ 0.218: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.53e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.80e-03 ) ; + Line search @ 0.284: ( Rflow ) = ( 1.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.142: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-01 ) ; + Last LinSolve(iter,res) = ( 13, 8.12e-03 ) ; + Line search @ 0.362: ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.181: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.66e-03 ) ; + Line search @ 0.458: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.71e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.04e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-05 ) ; + Last LinSolve(iter,res) = ( 10, 8.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.02421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.370671 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.78457e+07, 1.78848e+07, 1.79214e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.34867e+06, 5.4243e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.649 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.71141, 724.937 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3426.14, 702714 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 533.72, 213078 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2892.42, 489636 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 173.147, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3253, 702714 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3426.14, 0 }, { 996.523, 701697 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78249e+07, 1.78395e+07, 1.78644e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.3206e+06, 5.36733e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.839 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.311823, 223.527 } rm^3 +compflowStatistics, caprock: Phase mass: { 138.449, 216637 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 69.3191, 65082.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 69.1296, 151555 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.2632, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 128.186, 216637 } kg +compflowStatistics, caprock: Dissolved component mass: { { 138.449, 0 }, { 169.614, 216464 } } kg +compflowStatistics: Max phase CFL number: 5.34059 +compflowStatistics: Max component CFL number: 3.27776 +Time: 1.62e+08s, dt:1e+06s, Cycle: 1056 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.40e-03 ) ; + Line search @ 0.138: ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.64e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.86e-03 ) ; + Line search @ 0.165: ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.30e-03 ) ; + Line search @ 0.219: ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.110: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.89e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.90e-03 ) ; + Line search @ 0.247: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.123: ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-01 ) ; + Last LinSolve(iter,res) = ( 13, 6.97e-03 ) ; + Line search @ 0.266: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.133: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.84e-03 ) ; + Line search @ 0.293: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.147: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.49e-01 ) ; + Last LinSolve(iter,res) = ( 13, 6.88e-03 ) ; + Line search @ 0.358: ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.179: ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.089: ( Rflow ) = ( 9.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.39e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e+00 ) ; + Last LinSolve(iter,res) = ( 13, 6.94e-03 ) ; + Line search @ 0.399: ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.199: ( Rflow ) = ( 9.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.80e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.19e-03 ) ; + Line search @ 0.231: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.115: ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.16e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.27e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 4.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.57e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 1.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 16 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 9, 9.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 17 + ( Rflow ) = ( 4.55e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.55e-06 ) ; + Last LinSolve(iter,res) = ( 13, 2.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0154578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.328579 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78431e+07, 1.78821e+07, 1.79187e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.34573e+06, 5.42136e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.647 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.7006, 724.946 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3420.61, 702722 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 534.951, 213077 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2885.66, 489644 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 172.522, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3248.09, 702722 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3420.61, 0 }, { 1000.05, 701701 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78248e+07, 1.78373e+07, 1.78618e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.32488e+06, 5.3644e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.838 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.315037, 223.523 } rm^3 +compflowStatistics, caprock: Phase mass: { 139.85, 216633 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 69.7013, 65082.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 70.1488, 151551 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.1564, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 129.694, 216633 } kg +compflowStatistics, caprock: Dissolved component mass: { { 139.85, 0 }, { 170.22, 216460 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 7.30599 +compflowStatistics: Max component CFL number: 3.60583 +Time: 1.63e+08s, dt:1e+06s, Cycle: 1057 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-01 ) ; + Last LinSolve(iter,res) = ( 13, 8.50e-03 ) ; + Line search @ 0.166: ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.41e-03 ) ; + Line search @ 0.205: ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.33e-01 ) ; + Last LinSolve(iter,res) = ( 13, 7.25e-03 ) ; + Line search @ 0.288: ( Rflow ) = ( 2.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.144: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.58e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.77e-03 ) ; + Line search @ 0.337: ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.168: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.084: ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.80e-03 ) ; + Line search @ 0.351: ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.176: ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.37e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.59e-03 ) ; + Line search @ 0.411: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.206: ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.07e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.45e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.45e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0145969 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.30112 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78406e+07, 1.78797e+07, 1.79163e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.34311e+06, 5.41875e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.645 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.69004, 724.955 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3415.24, 702730 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 536.169, 213077 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2879.07, 489653 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 171.683, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3243.55, 702730 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3415.24, 0 }, { 1003.4, 701706 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78223e+07, 1.78349e+07, 1.78593e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.32481e+06, 5.36179e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.838 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.318259, 223.52 } rm^3 +compflowStatistics, caprock: Phase mass: { 141.256, 216630 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 70.0838, 65082.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 71.1724, 151547 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.1786, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 131.078, 216630 } kg +compflowStatistics, caprock: Dissolved component mass: { { 141.256, 0 }, { 170.842, 216455 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.83815 +compflowStatistics: Max component CFL number: 5.76354 +Time: 1.64e+08s, dt:1e+06s, Cycle: 1058 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.88e-03 ) ; + Line search @ 0.195: ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.48e-03 ) ; + Line search @ 0.258: ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.129: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.14e-03 ) ; + Line search @ 0.316: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.08e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.69e-03 ) ; + Line search @ 0.416: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.208: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.06e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e+00 ) ; + Last LinSolve(iter,res) = ( 12, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.06e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.46e-01 ) ; + Last LinSolve(iter,res) = ( 13, 5.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-01 ) ; + Last LinSolve(iter,res) = ( 13, 5.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-01 ) ; + Last LinSolve(iter,res) = ( 13, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 13, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.23e-02 ) ; + Last LinSolve(iter,res) = ( 13, 5.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.45e-02 ) ; + Last LinSolve(iter,res) = ( 12, 9.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 4.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.95e-03 ) ; + Last LinSolve(iter,res) = ( 12, 9.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 9.12e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.12e-06 ) ; + Last LinSolve(iter,res) = ( 10, 9.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0137234 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.291353 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78383e+07, 1.78774e+07, 1.7914e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.34065e+06, 5.41629e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.643 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.67985, 724.963 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3410.06, 702737 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 537.388, 213076 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2872.68, 489661 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 170.945, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3239.12, 702737 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3410.06, 0 }, { 1006.51, 701710 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.782e+07, 1.78326e+07, 1.7857e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.32235e+06, 5.35933e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.837 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.321501, 223.516 } rm^3 +compflowStatistics, caprock: Phase mass: { 142.672, 216626 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 70.4641, 65082.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 72.2076, 151544 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.0464, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 132.625, 216626 } kg +compflowStatistics, caprock: Dissolved component mass: { { 142.672, 0 }, { 171.481, 216451 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.91802 +compflowStatistics: Max component CFL number: 7.26474 +Time: 1.65e+08s, dt:1e+06s, Cycle: 1059 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.85e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.14e-03 ) ; + Line search @ 0.184: ( Rflow ) = ( 2.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.092: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.41e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.41e+00 ) ; + Last LinSolve(iter,res) = ( 13, 5.38e-03 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.063: ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.73e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e+00 ) ; + Last LinSolve(iter,res) = ( 12, 9.36e-03 ) ; + Line search @ 0.278: ( Rflow ) = ( 7.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.139: ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.070: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.035: ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.69e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.79e-03 ) ; + Line search @ 0.288: ( Rflow ) = ( 3.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.144: ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-01 ) ; + Last LinSolve(iter,res) = ( 14, 9.84e-03 ) ; + Line search @ 0.354: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.74e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.39e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.91e-02 ) ; + Last LinSolve(iter,res) = ( 11, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-02 ) ; + Last LinSolve(iter,res) = ( 12, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-04 ) ; + Last LinSolve(iter,res) = ( 9, 4.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0133249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.304133 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78361e+07, 1.78751e+07, 1.79117e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.33833e+06, 5.41397e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.642 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.66983, 724.972 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3404.99, 702745 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 538.492, 213075 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2866.49, 489670 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 170.016, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3234.97, 702745 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3404.99, 0 }, { 1009.51, 701715 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78177e+07, 1.78304e+07, 1.78548e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.32e+06, 5.35701e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.837 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.324761, 223.512 } rm^3 +compflowStatistics, caprock: Phase mass: { 144.096, 216622 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 70.8428, 65081.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 73.2529, 151540 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.86623, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 134.23, 216622 } kg +compflowStatistics, caprock: Dissolved component mass: { { 144.096, 0 }, { 172.132, 216446 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.91843 +compflowStatistics: Max component CFL number: 6.86647 +Time: 1.66e+08s, dt:1e+06s, Cycle: 1060 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-01 ) ; + Last LinSolve(iter,res) = ( 12, 6.78e-03 ) ; + Line search @ 0.239: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.16e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.10e-03 ) ; + Line search @ 0.340: ( Rflow ) = ( 8.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.08e-01 ) ; + Last LinSolve(iter,res) = ( 12, 6.82e-03 ) ; + Line search @ 0.329: ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.85e-02 ) ; + Last LinSolve(iter,res) = ( 11, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 11, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0132092 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.287836 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78338e+07, 1.78729e+07, 1.79095e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.33607e+06, 5.41173e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.64 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.65985, 724.98 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3399.94, 702752 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 539.528, 213075 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2860.41, 489678 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 169.126, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3230.81, 702752 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3399.94, 0 }, { 1012.47, 701719 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78155e+07, 1.78281e+07, 1.78525e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.31772e+06, 5.35475e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.836 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.328033, 223.508 } rm^3 +compflowStatistics, caprock: Phase mass: { 145.525, 216618 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 71.2197, 65081.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 74.3049, 151536 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.77661, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 135.748, 216618 } kg +compflowStatistics, caprock: Dissolved component mass: { { 145.525, 0 }, { 172.798, 216442 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.36657 +compflowStatistics: Max component CFL number: 5.90376 +Time: 1.67e+08s, dt:1e+06s, Cycle: 1061 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.40e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.29e-03 ) ; + Line search @ 0.191: ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.095: ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e+00 ) ; + Last LinSolve(iter,res) = ( 12, 9.29e-03 ) ; + Line search @ 0.242: ( Rflow ) = ( 4.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.121: ( Rflow ) = ( 2.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.061: ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e+00 ) ; + Last LinSolve(iter,res) = ( 12, 8.65e-03 ) ; + Line search @ 0.374: ( Rflow ) = ( 7.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.187: ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.094: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e+00 ) ; + Last LinSolve(iter,res) = ( 12, 9.03e-03 ) ; + Line search @ 0.416: ( Rflow ) = ( 1.11e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.208: ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.104: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.052: ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.44e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e+00 ) ; + Last LinSolve(iter,res) = ( 12, 8.69e-03 ) ; + Line search @ 0.355: ( Rflow ) = ( 9.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.178: ( Rflow ) = ( 3.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.089: ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.044: ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.23e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.42e-03 ) ; + Line search @ 0.363: ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.181: ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-01 ) ; + Last LinSolve(iter,res) = ( 12, 6.77e-03 ) ; + Line search @ 0.461: ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.52e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.31e-02 ) ; + Last LinSolve(iter,res) = ( 11, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.66e-02 ) ; + Last LinSolve(iter,res) = ( 11, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 11, 7.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 8, 8.62e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0128329 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.266242 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78316e+07, 1.78707e+07, 1.79073e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.33383e+06, 5.40949e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.638 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.65004, 724.988 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3394.99, 702760 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 540.418, 213074 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2854.57, 489686 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 168.11, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3226.88, 702760 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3394.99, 0 }, { 1015.3, 701724 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78133e+07, 1.78259e+07, 1.78503e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.31547e+06, 5.35251e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.836 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.331316, 223.505 } rm^3 +compflowStatistics, caprock: Phase mass: { 146.959, 216614 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 71.5937, 65081.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 75.3648, 151533 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.72364, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 137.235, 216614 } kg +compflowStatistics, caprock: Dissolved component mass: { { 146.959, 0 }, { 173.482, 216437 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.1015 +compflowStatistics: Max component CFL number: 5.46382 +Time: 1.68e+08s, dt:1e+06s, Cycle: 1062 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.84e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.49e-03 ) ; + Line search @ 0.231: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.47e-01 ) ; + Last LinSolve(iter,res) = ( 11, 9.87e-03 ) ; + Line search @ 0.371: ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.185: ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.093: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-01 ) ; + Last LinSolve(iter,res) = ( 11, 9.68e-03 ) ; + Line search @ 0.400: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.200: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.06e-01 ) ; + Last LinSolve(iter,res) = ( 11, 9.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.25e-01 ) ; + Last LinSolve(iter,res) = ( 11, 9.32e-03 ) ; + Line search @ 0.449: ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.225: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.112: ( Rflow ) = ( 8.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.26e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.53e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.41e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.62e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-05 ) ; + Last LinSolve(iter,res) = ( 9, 6.01e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0130107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.26266 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78294e+07, 1.78685e+07, 1.79051e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.33165e+06, 5.40732e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.637 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.64014, 724.997 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3389.99, 702767 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 541.132, 213073 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2848.86, 489694 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 167.043, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3222.95, 702767 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3389.99, 0 }, { 1018.16, 701728 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78111e+07, 1.78237e+07, 1.78481e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.31328e+06, 5.35033e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.835 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.334603, 223.501 } rm^3 +compflowStatistics, caprock: Phase mass: { 148.394, 216610 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 71.9633, 65081.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 76.4302, 151529 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.59872, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 138.795, 216610 } kg +compflowStatistics, caprock: Dissolved component mass: { { 148.394, 0 }, { 174.182, 216433 } } kg +compflowStatistics: Max phase CFL number: 4.15919 +compflowStatistics: Max component CFL number: 5.20893 +Time: 1.69e+08s, dt:1e+06s, Cycle: 1063 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.99e-01 ) ; + Last LinSolve(iter,res) = ( 11, 5.66e-03 ) ; + Line search @ 0.432: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.216: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 11, 7.31e-03 ) ; + Line search @ 0.482: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.241: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e+00 ) ; + Last LinSolve(iter,res) = ( 11, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.86e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.92e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 8.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.02e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.38e-02 ) ; + Last LinSolve(iter,res) = ( 10, 8.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 8.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.30e-03 ) ; + Last LinSolve(iter,res) = ( 11, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0131284 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.249513 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78272e+07, 1.78663e+07, 1.79029e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.32943e+06, 5.40512e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.635 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.63018, 725.005 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3384.97, 702775 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 541.851, 213073 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2843.12, 489702 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 166.305, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3218.66, 702775 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3384.97, 0 }, { 1021.04, 701733 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78088e+07, 1.78215e+07, 1.78459e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.31107e+06, 5.34812e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.835 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.337894, 223.497 } rm^3 +compflowStatistics, caprock: Phase mass: { 149.829, 216606 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 72.3308, 65081.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 77.4984, 151525 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.57026, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 140.259, 216606 } kg +compflowStatistics, caprock: Dissolved component mass: { { 149.829, 0 }, { 174.896, 216428 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.64256 +compflowStatistics: Max component CFL number: 4.90238 +Time: 1.7e+08s, dt:1e+06s, Cycle: 1064 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.26e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.92e-03 ) ; + Line search @ 0.213: ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.107: ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e+00 ) ; + Last LinSolve(iter,res) = ( 10, 8.60e-03 ) ; + Line search @ 0.253: ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.126: ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.37e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.04e-03 ) ; + Line search @ 0.313: ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.156: ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.078: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.17e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e+00 ) ; + Last LinSolve(iter,res) = ( 10, 8.19e-03 ) ; + Line search @ 0.340: ( Rflow ) = ( 4.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.170: ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.085: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.043: ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.23e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e+00 ) ; + Last LinSolve(iter,res) = ( 10, 7.82e-03 ) ; + Line search @ 0.359: ( Rflow ) = ( 5.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.179: ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.090: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.80e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.43e-03 ) ; + Line search @ 0.394: ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.197: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.81e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.74e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.41e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.98e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.39e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 8.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.17e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 8.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.25e-02 ) ; + Last LinSolve(iter,res) = ( 10, 7.44e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 8.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.92e-03 ) ; + Last LinSolve(iter,res) = ( 10, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 15 + ( Rflow ) = ( 5.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-04 ) ; + Last LinSolve(iter,res) = ( 9, 7.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0130314 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.318043 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.7825e+07, 1.7864e+07, 1.79007e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.32719e+06, 5.40289e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.634 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.62024, 725.013 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3379.97, 702782 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 542.55, 213072 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2837.42, 489710 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 165.486, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3214.48, 702782 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3379.97, 0 }, { 1023.87, 701738 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78066e+07, 1.78193e+07, 1.78437e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.30884e+06, 5.34588e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.834 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.341193, 223.493 } rm^3 +compflowStatistics, caprock: Phase mass: { 151.268, 216602 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 72.6982, 65080.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 78.5701, 151522 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.6118, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 141.657, 216602 } kg +compflowStatistics, caprock: Dissolved component mass: { { 151.268, 0 }, { 175.625, 216423 } } kg +compflowStatistics: Max phase CFL number: 5.71483 +compflowStatistics: Max component CFL number: 4.4995 +Time: 1.71e+08s, dt:1e+06s, Cycle: 1065 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.27e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.26e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e+00 ) ; + Last LinSolve(iter,res) = ( 10, 6.49e-03 ) ; + Line search @ 0.253: ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.126: ( Rflow ) = ( 5.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.063: ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.032: ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e+00 ) ; + Last LinSolve(iter,res) = ( 10, 6.79e-03 ) ; + Line search @ 0.252: ( Rflow ) = ( 4.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.126: ( Rflow ) = ( 2.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.063: ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.032: ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e+00 ) ; + Last LinSolve(iter,res) = ( 10, 6.48e-03 ) ; + Line search @ 0.254: ( Rflow ) = ( 5.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.127: ( Rflow ) = ( 3.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.063: ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.032: ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.88e-03 ) ; + Line search @ 0.256: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.96e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.88e-03 ) ; + Line search @ 0.356: ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.178: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.17e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e+00 ) ; + Last LinSolve(iter,res) = ( 10, 6.47e-03 ) ; + Line search @ 0.492: ( Rflow ) = ( 3.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.246: ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.123: ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e+00 ) ; + Last LinSolve(iter,res) = ( 9, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.72e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.41e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.32e-04 ) ; + Last LinSolve(iter,res) = ( 9, 9.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0132463 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.246223 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.78227e+07, 1.78618e+07, 1.78984e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.32497e+06, 5.40067e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.632 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.61019, 725.022 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3374.91, 702790 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 543.215, 213071 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2831.7, 489719 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 164.478, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3210.43, 702790 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3374.91, 0 }, { 1026.74, 701742 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78044e+07, 1.7817e+07, 1.78414e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.30661e+06, 5.34366e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.834 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.344496, 223.489 } rm^3 +compflowStatistics, caprock: Phase mass: { 152.708, 216599 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 73.0606, 65080.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 79.6478, 151518 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.42642, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 143.282, 216599 } kg +compflowStatistics, caprock: Dissolved component mass: { { 152.708, 0 }, { 176.366, 216419 } } kg +compflowStatistics: Max phase CFL number: 5.13275 +compflowStatistics: Max component CFL number: 4.31432 +Time: 1.72e+08s, dt:1e+06s, Cycle: 1066 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e+00 ) ; + Last LinSolve(iter,res) = ( 10, 7.30e-03 ) ; + Line search @ 0.296: ( Rflow ) = ( 5.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.148: ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.074: ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.037: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e+00 ) ; + Last LinSolve(iter,res) = ( 10, 6.76e-03 ) ; + Line search @ 0.307: ( Rflow ) = ( 5.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.154: ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.077: ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.038: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.39e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.89e-03 ) ; + Line search @ 0.322: ( Rflow ) = ( 3.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.161: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.79e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.70e-03 ) ; + Line search @ 0.382: ( Rflow ) = ( 2.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.191: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.34e-03 ) ; + Line search @ 0.475: ( Rflow ) = ( 2.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.238: ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.42e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 7.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.95e-02 ) ; + Last LinSolve(iter,res) = ( 9, 9.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 5.49e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.49e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0129572 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.269336 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78205e+07, 1.78596e+07, 1.78962e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.3227e+06, 5.39841e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.63 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.60026, 725.03 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3369.93, 702797 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 543.92, 213071 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2826.01, 489727 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 163.685, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3206.24, 702797 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3369.93, 0 }, { 1029.53, 701747 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78021e+07, 1.78148e+07, 1.78392e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.30435e+06, 5.34139e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.833 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.347814, 223.486 } rm^3 +compflowStatistics, caprock: Phase mass: { 154.155, 216595 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 73.4238, 65080.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 80.731, 151514 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.41657, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 144.738, 216595 } kg +compflowStatistics, caprock: Dissolved component mass: { { 154.155, 0 }, { 177.119, 216414 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.46297 +compflowStatistics: Max component CFL number: 4.34936 +Time: 1.73e+08s, dt:1e+06s, Cycle: 1067 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.73e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.02e-03 ) ; + Line search @ 0.233: ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.116: ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.058: ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.00e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.20e-03 ) ; + Line search @ 0.243: ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.121: ( Rflow ) = ( 2.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.061: ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.79e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.56e-03 ) ; + Line search @ 0.287: ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.143: ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.26e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e+00 ) ; + Last LinSolve(iter,res) = ( 10, 6.20e-03 ) ; + Line search @ 0.340: ( Rflow ) = ( 6.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.170: ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.085: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.042: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.67e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.71e-03 ) ; + Line search @ 0.412: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.206: ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.93e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 7.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.58e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 2.91e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.91e-05 ) ; + Last LinSolve(iter,res) = ( 10, 8.81e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.012514 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.285815 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78183e+07, 1.78574e+07, 1.78941e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.32048e+06, 5.3962e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.629 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.59055, 725.038 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3365.06, 702805 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 544.643, 213070 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2820.42, 489735 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 162.877, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3202.19, 702805 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3365.06, 0 }, { 1032.17, 701752 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.78e+07, 1.78126e+07, 1.7837e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.30212e+06, 5.33918e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.833 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.351147, 223.482 } rm^3 +compflowStatistics, caprock: Phase mass: { 155.609, 216591 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 73.7875, 65080.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 81.8212, 151510 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.36502, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 146.244, 216591 } kg +compflowStatistics, caprock: Dissolved component mass: { { 155.609, 0 }, { 177.885, 216409 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 6.36895 +compflowStatistics: Max component CFL number: 3.74328 +Time: 1.74e+08s, dt:1e+06s, Cycle: 1068 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.86e-01 ) ; + Last LinSolve(iter,res) = ( 11, 7.30e-03 ) ; + Line search @ 0.227: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.49e-03 ) ; + Line search @ 0.351: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.175: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.90e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.45e-03 ) ; + Line search @ 0.467: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.233: ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.117: ( Rflow ) = ( 9.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.24e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.39e-03 ) ; + Line search @ 0.493: ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.246: ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.16e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.53e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 5.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 2.12e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0122972 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.277417 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78162e+07, 1.78553e+07, 1.7892e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.31834e+06, 5.39406e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.627 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.58094, 725.046 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3360.26, 702812 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 545.247, 213069 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2815.01, 489743 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 162.176, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3198.08, 702812 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3360.26, 0 }, { 1034.74, 701756 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77978e+07, 1.78105e+07, 1.78349e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.29996e+06, 5.33703e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.832 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.35449, 223.478 } rm^3 +compflowStatistics, caprock: Phase mass: { 157.067, 216587 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 74.1485, 65080.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 82.9182, 151507 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.28403, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 147.783, 216587 } kg +compflowStatistics, caprock: Dissolved component mass: { { 157.067, 0 }, { 178.667, 216405 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.41169 +compflowStatistics: Max component CFL number: 3.45551 +Time: 1.75e+08s, dt:1e+06s, Cycle: 1069 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.03e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.62e-03 ) ; + Line search @ 0.237: ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.08e-03 ) ; + Line search @ 0.315: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.59e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.35e-03 ) ; + Line search @ 0.455: ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.228: ( Rflow ) = ( 9.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.95e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.35e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.55e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.62e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-06 ) ; + Last LinSolve(iter,res) = ( 12, 5.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0119363 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.346151 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78142e+07, 1.78533e+07, 1.78899e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.31623e+06, 5.39197e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.626 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.57152, 725.054 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3355.56, 702819 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 545.837, 213069 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2809.72, 489751 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 161.402, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3194.16, 702819 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3355.56, 0 }, { 1037.17, 701761 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77958e+07, 1.78084e+07, 1.78329e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.29785e+06, 5.33493e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.832 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.357846, 223.474 } rm^3 +compflowStatistics, caprock: Phase mass: { 158.531, 216583 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 74.509, 65080 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 84.0218, 151503 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.31836, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 149.212, 216583 } kg +compflowStatistics, caprock: Dissolved component mass: { { 158.531, 0 }, { 179.464, 216400 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.91003 +compflowStatistics: Max component CFL number: 3.21772 +Time: 1.76e+08s, dt:1e+06s, Cycle: 1070 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e+00 ) ; + Last LinSolve(iter,res) = ( 9, 7.66e-03 ) ; + Line search @ 0.280: ( Rflow ) = ( 3.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.140: ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.67e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e+00 ) ; + Last LinSolve(iter,res) = ( 9, 7.89e-03 ) ; + Line search @ 0.314: ( Rflow ) = ( 8.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.157: ( Rflow ) = ( 3.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.079: ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.039: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e+00 ) ; + Last LinSolve(iter,res) = ( 9, 7.48e-03 ) ; + Line search @ 0.327: ( Rflow ) = ( 3.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.164: ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.99e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.40e-03 ) ; + Line search @ 0.388: ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.194: ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.17e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.52e-03 ) ; + Line search @ 0.415: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.08e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.85e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.27e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-05 ) ; + Last LinSolve(iter,res) = ( 10, 8.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0114576 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.305645 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78122e+07, 1.78513e+07, 1.7888e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.31419e+06, 5.38993e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.624 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.56234, 725.062 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3350.99, 702826 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 546.452, 213068 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2804.54, 489758 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 160.678, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3190.31, 702826 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3350.99, 0 }, { 1039.46, 701766 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77938e+07, 1.78064e+07, 1.78309e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.29579e+06, 5.33289e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.832 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.361227, 223.47 } rm^3 +compflowStatistics, caprock: Phase mass: { 160.006, 216579 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 74.8719, 65079.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 85.1342, 151499 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.23762, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 150.769, 216579 } kg +compflowStatistics, caprock: Dissolved component mass: { { 160.006, 0 }, { 180.267, 216395 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.86395 +compflowStatistics: Max component CFL number: 3.26146 +Time: 1.77e+08s, dt:1e+06s, Cycle: 1071 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.07e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e+00 ) ; + Last LinSolve(iter,res) = ( 9, 7.00e-03 ) ; + Line search @ 0.314: ( Rflow ) = ( 3.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.157: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e+00 ) ; + Last LinSolve(iter,res) = ( 9, 7.53e-03 ) ; + Line search @ 0.375: ( Rflow ) = ( 2.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.188: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.93e-03 ) ; + Line search @ 0.324: ( Rflow ) = ( 3.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.162: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.32e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.70e-03 ) ; + Line search @ 0.416: ( Rflow ) = ( 5.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.208: ( Rflow ) = ( 2.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.104: ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.052: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.12e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.74e-03 ) ; + Line search @ 0.447: ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.224: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.90e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.97e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.21e-03 ) ; + Last LinSolve(iter,res) = ( 9, 7.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.89e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0113265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.274199 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78103e+07, 1.78494e+07, 1.78861e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.31224e+06, 5.38799e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.623 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.55324, 725.07 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3346.47, 702833 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 546.932, 213068 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2799.54, 489766 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 159.917, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3186.55, 702833 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3346.47, 0 }, { 1041.69, 701770 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77919e+07, 1.78045e+07, 1.7829e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.29382e+06, 5.33094e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.831 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.364618, 223.467 } rm^3 +compflowStatistics, caprock: Phase mass: { 161.486, 216575 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 75.2323, 65079.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 86.2539, 151496 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.0717, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 152.415, 216575 } kg +compflowStatistics, caprock: Dissolved component mass: { { 161.486, 0 }, { 181.081, 216391 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.12796 +compflowStatistics: Max component CFL number: 3.16284 +Time: 1.78e+08s, dt:1e+06s, Cycle: 1072 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e+00 ) ; + Last LinSolve(iter,res) = ( 10, 9.18e-03 ) ; + Line search @ 0.224: ( Rflow ) = ( 5.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.112: ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.056: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-01 ) ; + Last LinSolve(iter,res) = ( 10, 9.22e-03 ) ; + Line search @ 0.248: ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.02e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e+00 ) ; + Last LinSolve(iter,res) = ( 11, 9.58e-03 ) ; + Line search @ 0.416: ( Rflow ) = ( 4.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.208: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.104: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.61e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.61e+00 ) ; + Last LinSolve(iter,res) = ( 12, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.51e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e+00 ) ; + Last LinSolve(iter,res) = ( 12, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e+00 ) ; + Last LinSolve(iter,res) = ( 12, 7.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.05e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 9.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.23e-02 ) ; + Last LinSolve(iter,res) = ( 12, 7.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.79e-03 ) ; + Last LinSolve(iter,res) = ( 12, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 7.74e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.74e-05 ) ; + Last LinSolve(iter,res) = ( 10, 7.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0112927 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.241478 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78084e+07, 1.78475e+07, 1.78842e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.31032e+06, 5.38607e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.622 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.54416, 725.077 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3341.96, 702840 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 547.279, 213067 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2794.68, 489773 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 159.094, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3182.87, 702840 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3341.96, 0 }, { 1043.89, 701775 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.779e+07, 1.78026e+07, 1.78271e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.29188e+06, 5.32902e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.831 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.368015, 223.463 } rm^3 +compflowStatistics, caprock: Phase mass: { 162.969, 216572 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 75.5904, 65079.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 87.3784, 151492 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.07285, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 153.896, 216572 } kg +compflowStatistics, caprock: Dissolved component mass: { { 162.969, 0 }, { 181.908, 216386 } } kg +compflowStatistics: Max phase CFL number: 4.40338 +compflowStatistics: Max component CFL number: 3.30614 +Time: 1.79e+08s, dt:1e+06s, Cycle: 1073 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.72e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.28e-03 ) ; + Line search @ 0.205: ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.103: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.18e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e+00 ) ; + Last LinSolve(iter,res) = ( 12, 5.55e-03 ) ; + Line search @ 0.238: ( Rflow ) = ( 5.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.119: ( Rflow ) = ( 2.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.060: ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.50e-01 ) ; + Last LinSolve(iter,res) = ( 18, 7.66e-03 ) ; + Line search @ 0.332: ( Rflow ) = ( 3.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.166: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.083: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.68e-01 ) ; + Last LinSolve(iter,res) = ( 12, 7.24e-03 ) ; + Line search @ 0.363: ( Rflow ) = ( 4.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.181: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.091: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.045: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-01 ) ; + Last LinSolve(iter,res) = ( 12, 5.56e-03 ) ; + Line search @ 0.381: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.190: ( Rflow ) = ( 1.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.97e-03 ) ; + Line search @ 0.464: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.232: ( Rflow ) = ( 8.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-01 ) ; + Last LinSolve(iter,res) = ( 11, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 3.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.40e-01 ) ; + Last LinSolve(iter,res) = ( 11, 7.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.39e-01 ) ; + Last LinSolve(iter,res) = ( 11, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.56e-02 ) ; + Last LinSolve(iter,res) = ( 11, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 6.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.69e-02 ) ; + Last LinSolve(iter,res) = ( 11, 5.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-02 ) ; + Last LinSolve(iter,res) = ( 11, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 14 + ( Rflow ) = ( 1.72e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0108609 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.280336 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78066e+07, 1.78457e+07, 1.78823e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.3084e+06, 5.38416e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.62 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.5353, 725.085 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3337.57, 702847 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 547.614, 213066 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2789.96, 489780 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 158.521, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3179.05, 702847 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3337.57, 0 }, { 1045.95, 701780 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77881e+07, 1.78007e+07, 1.78253e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.28996e+06, 5.32711e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.83 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.371427, 223.459 } rm^3 +compflowStatistics, caprock: Phase mass: { 164.458, 216568 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 75.9483, 65079.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 88.5098, 151488 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.00809, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 155.45, 216568 } kg +compflowStatistics, caprock: Dissolved component mass: { { 164.458, 0 }, { 182.747, 216381 } } kg +compflowStatistics: Max phase CFL number: 3.53049 +compflowStatistics: Max component CFL number: 3.33917 +Time: 1.8e+08s, dt:1e+06s, Cycle: 1074 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.42e-01 ) ; + Last LinSolve(iter,res) = ( 11, 7.05e-03 ) ; + Line search @ 0.322: ( Rflow ) = ( 2.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.161: ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e+00 ) ; + Last LinSolve(iter,res) = ( 11, 6.82e-03 ) ; + Line search @ 0.382: ( Rflow ) = ( 4.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.191: ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.095: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-01 ) ; + Last LinSolve(iter,res) = ( 11, 5.95e-03 ) ; + Line search @ 0.435: ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 8, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.53e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.53e-05 ) ; + Last LinSolve(iter,res) = ( 9, 5.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0103788 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.2488 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78048e+07, 1.78439e+07, 1.78806e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.30656e+06, 5.38233e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.619 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.52667, 725.092 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3333.32, 702853 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 548.009, 213066 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2785.31, 489788 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 157.926, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3175.39, 702853 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3333.32, 0 }, { 1047.86, 701784 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77863e+07, 1.77989e+07, 1.78235e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2881e+06, 5.32527e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.83 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.374856, 223.455 } rm^3 +compflowStatistics, caprock: Phase mass: { 165.955, 216564 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 76.3076, 65079.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 89.6479, 151485 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.05813, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 156.897, 216564 } kg +compflowStatistics, caprock: Dissolved component mass: { { 165.955, 0 }, { 183.599, 216377 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.85478 +compflowStatistics: Max component CFL number: 3.2288 +Time: 1.81e+08s, dt:1e+06s, Cycle: 1075 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.59e-03 ) ; + Line search @ 0.265: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.11e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.89e-03 ) ; + Line search @ 0.365: ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.183: ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.091: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.046: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.89e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.44e-03 ) ; + Line search @ 0.388: ( Rflow ) = ( 3.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.194: ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.097: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.049: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.15e-01 ) ; + Last LinSolve(iter,res) = ( 9, 8.93e-03 ) ; + Line search @ 0.417: ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.208: ( Rflow ) = ( 9.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.38e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.53e-01 ) ; + Last LinSolve(iter,res) = ( 9, 9.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 10, 8.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 10, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 10, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.90e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0101382 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.244547 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78031e+07, 1.78422e+07, 1.78789e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.30481e+06, 5.38058e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.618 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.51817, 725.1 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3329.13, 702860 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 548.298, 213065 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2780.83, 489795 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 157.251, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3171.88, 702860 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3329.13, 0 }, { 1049.68, 701789 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77846e+07, 1.77972e+07, 1.78218e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.28633e+06, 5.32352e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.83 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.378299, 223.451 } rm^3 +compflowStatistics, caprock: Phase mass: { 167.46, 216560 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 76.6668, 65079.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 90.7929, 151481 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.99444, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 158.465, 216560 } kg +compflowStatistics, caprock: Dissolved component mass: { { 167.46, 0 }, { 184.459, 216372 } } kg +compflowStatistics: Max phase CFL number: 4.60452 +compflowStatistics: Max component CFL number: 3.16575 +Time: 1.82e+08s, dt:1e+06s, Cycle: 1076 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e+00 ) ; + Last LinSolve(iter,res) = ( 10, 7.78e-03 ) ; + Line search @ 0.261: ( Rflow ) = ( 7.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.131: ( Rflow ) = ( 3.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.065: ( Rflow ) = ( 2.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.033: ( Rflow ) = ( 1.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e+00 ) ; + Last LinSolve(iter,res) = ( 10, 7.50e-03 ) ; + Line search @ 0.271: ( Rflow ) = ( 7.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.136: ( Rflow ) = ( 4.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.068: ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.034: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-01 ) ; + Last LinSolve(iter,res) = ( 10, 7.50e-03 ) ; + Line search @ 0.282: ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.09e-01 ) ; + Last LinSolve(iter,res) = ( 9, 7.38e-03 ) ; + Line search @ 0.445: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-02 ) ; + Last LinSolve(iter,res) = ( 9, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.93e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.33e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.33e-05 ) ; + Last LinSolve(iter,res) = ( 10, 2.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0104118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.249583 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.78013e+07, 1.78405e+07, 1.78771e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.3031e+06, 5.37888e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.616 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.50954, 725.107 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3324.88, 702867 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 548.425, 213065 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2776.45, 489802 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 156.605, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3168.27, 702867 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3324.88, 0 }, { 1051.56, 701794 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77829e+07, 1.77954e+07, 1.78201e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.28461e+06, 5.32181e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.829 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.381746, 223.447 } rm^3 +compflowStatistics, caprock: Phase mass: { 168.964, 216556 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 77.0237, 65079 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 91.9406, 151477 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.93557, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 160.029, 216556 } kg +compflowStatistics, caprock: Dissolved component mass: { { 168.964, 0 }, { 185.326, 216367 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.37765 +compflowStatistics: Max component CFL number: 3.09195 +Time: 1.83e+08s, dt:1e+06s, Cycle: 1077 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.13e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e+00 ) ; + Last LinSolve(iter,res) = ( 9, 6.12e-03 ) ; + Line search @ 0.294: ( Rflow ) = ( 4.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.147: ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.074: ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e+00 ) ; + Last LinSolve(iter,res) = ( 8, 9.59e-03 ) ; + Line search @ 0.323: ( Rflow ) = ( 6.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.162: ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.081: ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.040: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.01e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.81e-03 ) ; + Line search @ 0.346: ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.87e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.88e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0104132 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.267914 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77996e+07, 1.78387e+07, 1.78754e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.30134e+06, 5.37713e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.615 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.50091, 725.114 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3320.63, 702873 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 548.593, 213064 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2772.03, 489809 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 156.179, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3164.45, 702873 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3320.63, 0 }, { 1053.43, 701799 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77811e+07, 1.77937e+07, 1.78183e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.28286e+06, 5.32006e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.829 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.385196, 223.444 } rm^3 +compflowStatistics, caprock: Phase mass: { 170.47, 216552 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 77.3775, 65078.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 93.0926, 151474 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.8755, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 161.595, 216552 } kg +compflowStatistics, caprock: Dissolved component mass: { { 170.47, 0 }, { 186.206, 216363 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.43782 +compflowStatistics: Max component CFL number: 2.87163 +Time: 1.84e+08s, dt:1e+06s, Cycle: 1078 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.82e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.58e-03 ) ; + Line search @ 0.121: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.63e-03 ) ; + Line search @ 0.281: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e+00 ) ; + Last LinSolve(iter,res) = ( 8, 9.86e-03 ) ; + Line search @ 0.451: ( Rflow ) = ( 4.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.226: ( Rflow ) = ( 8.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.33e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e+00 ) ; + Last LinSolve(iter,res) = ( 8, 8.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.80e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.85e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.01e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 2.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.49e-03 ) ; + Last LinSolve(iter,res) = ( 8, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 13 + ( Rflow ) = ( 3.01e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e-05 ) ; + Last LinSolve(iter,res) = ( 8, 8.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0102216 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.285086 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77979e+07, 1.7837e+07, 1.78737e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29959e+06, 5.37538e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.614 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.49236, 725.122 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3316.42, 702880 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 548.825, 213064 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2767.6, 489816 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 155.705, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3160.72, 702880 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3316.42, 0 }, { 1055.23, 701803 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77794e+07, 1.7792e+07, 1.78166e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.28111e+06, 5.3183e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.828 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.388655, 223.44 } rm^3 +compflowStatistics, caprock: Phase mass: { 171.98, 216549 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 77.7303, 65078.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 94.2496, 151470 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.88479, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 163.095, 216549 } kg +compflowStatistics, caprock: Dissolved component mass: { { 171.98, 0 }, { 187.094, 216358 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 6.90351 +compflowStatistics: Max component CFL number: 3.60473 +Time: 1.85e+08s, dt:1e+06s, Cycle: 1079 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.93e-01 ) ; + Last LinSolve(iter,res) = ( 8, 9.39e-03 ) ; + Line search @ 0.379: ( Rflow ) = ( 1.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.190: ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.21e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.89e-03 ) ; + Line search @ 0.462: ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.84e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 8, 9.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.15e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.02e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.02e-06 ) ; + Last LinSolve(iter,res) = ( 9, 4.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00983541 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.222129 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77962e+07, 1.78353e+07, 1.7872e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29786e+06, 5.37366e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.613 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.48398, 725.129 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3312.31, 702886 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 549.104, 213063 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2763.21, 489823 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 155.248, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3157.07, 702886 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3312.31, 0 }, { 1056.93, 701808 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77777e+07, 1.77903e+07, 1.78149e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27937e+06, 5.31658e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.828 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.392135, 223.436 } rm^3 +compflowStatistics, caprock: Phase mass: { 173.499, 216545 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 78.087, 65078.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 95.412, 151466 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.90796, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 164.591, 216545 } kg +compflowStatistics, caprock: Dissolved component mass: { { 173.499, 0 }, { 187.987, 216353 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.28642 +compflowStatistics: Max component CFL number: 5.07701 +Time: 1.86e+08s, dt:1e+06s, Cycle: 1080 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.92e-03 ) ; + Line search @ 0.305: ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.152: ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.59e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.87e-03 ) ; + Line search @ 0.378: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.97e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00970337 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.290067 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77946e+07, 1.78337e+07, 1.78704e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29621e+06, 5.372e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.612 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.47565, 725.136 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3308.24, 702893 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 549.333, 213063 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2758.9, 489830 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 154.843, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3153.39, 702893 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3308.24, 0 }, { 1058.59, 701813 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77761e+07, 1.77886e+07, 1.78133e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2777e+06, 5.31492e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.828 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.395623, 223.432 } rm^3 +compflowStatistics, caprock: Phase mass: { 175.022, 216541 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 78.4419, 65078.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 96.5801, 151463 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.87312, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 166.149, 216541 } kg +compflowStatistics, caprock: Dissolved component mass: { { 175.022, 0 }, { 188.887, 216348 } } kg +compflowStatistics: Max phase CFL number: 4.86227 +compflowStatistics: Max component CFL number: 5.35257 +Time: 1.87e+08s, dt:1e+06s, Cycle: 1081 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.95e-03 ) ; + Line search @ 0.267: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e+00 ) ; + Last LinSolve(iter,res) = ( 8, 8.00e-03 ) ; + Line search @ 0.379: ( Rflow ) = ( 6.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.190: ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.19e-03 ) ; + Line search @ 0.471: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.236: ( Rflow ) = ( 7.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.26e-03 ) ; + Line search @ 0.422: ( Rflow ) = ( 7.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.211: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 8, 7.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-02 ) ; + Last LinSolve(iter,res) = ( 8, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.84e-02 ) ; + Last LinSolve(iter,res) = ( 8, 8.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.83e-02 ) ; + Last LinSolve(iter,res) = ( 9, 7.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 4.47e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.47e-03 ) ; + Last LinSolve(iter,res) = ( 11, 9.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 11, 7.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00940183 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.298306 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7793e+07, 1.78321e+07, 1.78688e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29457e+06, 5.37037e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.61 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.46747, 725.143 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3304.23, 702899 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 549.645, 213062 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2754.59, 489837 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 154.519, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3149.71, 702899 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3304.23, 0 }, { 1060.15, 701817 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.77745e+07, 1.7787e+07, 1.78117e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27606e+06, 5.31329e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.827 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.399127, 223.428 } rm^3 +compflowStatistics, caprock: Phase mass: { 176.552, 216537 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 78.7943, 65078.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 97.7577, 151459 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.67853, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 167.873, 216537 } kg +compflowStatistics, caprock: Dissolved component mass: { { 176.552, 0 }, { 189.793, 216344 } } kg +compflowStatistics: Max phase CFL number: 5.8776 +compflowStatistics: Max component CFL number: 4.66371 +Time: 1.88e+08s, dt:1e+06s, Cycle: 1082 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.92e-01 ) ; + Last LinSolve(iter,res) = ( 12, 8.46e-03 ) ; + Line search @ 0.230: ( Rflow ) = ( 3.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.115: ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.61e-01 ) ; + Last LinSolve(iter,res) = ( 12, 9.02e-03 ) ; + Line search @ 0.267: ( Rflow ) = ( 3.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.134: ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.07e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e+00 ) ; + Last LinSolve(iter,res) = ( 8, 9.21e-03 ) ; + Line search @ 0.314: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.157: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.34e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e+00 ) ; + Last LinSolve(iter,res) = ( 8, 8.41e-03 ) ; + Line search @ 0.380: ( Rflow ) = ( 4.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.190: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.095: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.13e-01 ) ; + Last LinSolve(iter,res) = ( 9, 5.46e-03 ) ; + Line search @ 0.429: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.215: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.23e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 8, 5.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00930147 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.328411 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77914e+07, 1.78305e+07, 1.78672e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29298e+06, 5.36878e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.609 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.45931, 725.15 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3300.25, 702905 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 549.951, 213062 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2750.3, 489844 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 154.254, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3145.99, 702905 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3300.25, 0 }, { 1061.69, 701822 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77729e+07, 1.77854e+07, 1.78101e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27446e+06, 5.3117e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.827 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.402641, 223.424 } rm^3 +compflowStatistics, caprock: Phase mass: { 178.087, 216533 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 79.1467, 65078.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 98.9399, 151455 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.64907, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 169.438, 216533 } kg +compflowStatistics, caprock: Dissolved component mass: { { 178.087, 0 }, { 190.704, 216339 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.28792 +compflowStatistics: Max component CFL number: 4.79967 +Time: 1.89e+08s, dt:1e+06s, Cycle: 1083 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.89e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.76e-03 ) ; + Line search @ 0.306: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.87e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.90e-03 ) ; + Line search @ 0.229: ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.114: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.057: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e+00 ) ; + Last LinSolve(iter,res) = ( 7, 9.25e-03 ) ; + Line search @ 0.338: ( Rflow ) = ( 5.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.169: ( Rflow ) = ( 2.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.085: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.042: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e+00 ) ; + Last LinSolve(iter,res) = ( 7, 9.00e-03 ) ; + Line search @ 0.476: ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.238: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.47e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e+00 ) ; + Last LinSolve(iter,res) = ( 7, 8.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.47e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e+00 ) ; + Last LinSolve(iter,res) = ( 7, 8.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e-01 ) ; + Last LinSolve(iter,res) = ( 7, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.72e-02 ) ; + Last LinSolve(iter,res) = ( 7, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.44e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-05 ) ; + Last LinSolve(iter,res) = ( 8, 3.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00917506 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.232276 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77899e+07, 1.7829e+07, 1.78657e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.29141e+06, 5.36721e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.608 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.45121, 725.157 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3296.29, 702911 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.241, 213061 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2746.05, 489850 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 153.688, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3142.61, 702911 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3296.29, 0 }, { 1063.19, 701827 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77713e+07, 1.77839e+07, 1.78086e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27288e+06, 5.31013e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.827 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.406162, 223.42 } rm^3 +compflowStatistics, caprock: Phase mass: { 179.624, 216530 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 79.4987, 65078.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 100.126, 151451 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.66513, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 170.959, 216530 } kg +compflowStatistics, caprock: Dissolved component mass: { { 179.624, 0 }, { 191.624, 216334 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.05113 +compflowStatistics: Max component CFL number: 4.62298 +Time: 1.9e+08s, dt:1e+06s, Cycle: 1084 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.57e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.64e-03 ) ; + Line search @ 0.270: ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.135: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.70e-03 ) ; + Line search @ 0.318: ( Rflow ) = ( 9.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.65e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00903835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.277075 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77883e+07, 1.78275e+07, 1.78641e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.28986e+06, 5.36566e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.607 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.44314, 725.164 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3292.36, 702918 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.463, 213061 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2741.9, 489857 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 153.38, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3138.98, 702918 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3292.36, 0 }, { 1064.65, 701832 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77698e+07, 1.77823e+07, 1.7807e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.27132e+06, 5.30858e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.826 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.409694, 223.417 } rm^3 +compflowStatistics, caprock: Phase mass: { 181.166, 216526 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 79.8505, 65078 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 101.316, 151448 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.69106, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 172.475, 216526 } kg +compflowStatistics, caprock: Dissolved component mass: { { 181.166, 0 }, { 192.548, 216329 } } kg +compflowStatistics: Max phase CFL number: 3.65988 +compflowStatistics: Max component CFL number: 4.11298 +Time: 1.91e+08s, dt:1e+06s, Cycle: 1085 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.17e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.91e-03 ) ; + Line search @ 0.287: ( Rflow ) = ( 4.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.144: ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.37e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.93e-03 ) ; + Line search @ 0.297: ( Rflow ) = ( 8.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.148: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-01 ) ; + Last LinSolve(iter,res) = ( 7, 6.02e-03 ) ; + Line search @ 0.426: ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.58e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.58e-05 ) ; + Last LinSolve(iter,res) = ( 7, 3.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00895647 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.251619 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77868e+07, 1.78259e+07, 1.78626e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.28832e+06, 5.36413e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.606 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.43509, 725.171 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3288.44, 702924 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.694, 213060 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2737.75, 489864 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 153.156, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3135.28, 702924 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3288.44, 0 }, { 1066.1, 701836 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77682e+07, 1.77808e+07, 1.78055e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26978e+06, 5.30704e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.826 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.413236, 223.413 } rm^3 +compflowStatistics, caprock: Phase mass: { 182.713, 216522 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 80.2025, 65077.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 102.51, 151444 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.6084, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 174.105, 216522 } kg +compflowStatistics, caprock: Dissolved component mass: { { 182.713, 0 }, { 193.474, 216325 } } kg +compflowStatistics: Max phase CFL number: 23.4775 +compflowStatistics: Max component CFL number: 3.50373 +Time: 1.92e+08s, dt:1e+06s, Cycle: 1086 +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.91e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.74e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.01e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.80e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00875102 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.268128 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77853e+07, 1.78244e+07, 1.78611e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.28679e+06, 5.3626e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.605 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.4271, 725.178 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3284.55, 702930 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.982, 213060 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2733.57, 489871 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.809, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3131.74, 702930 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3284.55, 0 }, { 1067.51, 701841 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77667e+07, 1.77793e+07, 1.7804e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26825e+06, 5.30551e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.826 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.416795, 223.409 } rm^3 +compflowStatistics, caprock: Phase mass: { 184.267, 216518 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 80.5557, 65077.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 103.711, 151440 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.54834, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 175.718, 216518 } kg +compflowStatistics, caprock: Dissolved component mass: { { 184.267, 0 }, { 194.4, 216320 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 39.0538 +compflowStatistics: Max component CFL number: 7.5875 +Time: 1.93e+08s, dt:1e+06s, Cycle: 1087 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.07e-01 ) ; + Last LinSolve(iter,res) = ( 6, 9.11e-03 ) ; + Line search @ 0.295: ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 8, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.87e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.25e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.72e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.72e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00858929 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.207958 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77838e+07, 1.78229e+07, 1.78596e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.28528e+06, 5.36109e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.604 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.41916, 725.185 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3280.69, 702936 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.241, 213059 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2729.45, 489877 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.493, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3128.2, 702936 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3280.69, 0 }, { 1068.88, 701846 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77652e+07, 1.77778e+07, 1.78025e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26674e+06, 5.304e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.825 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.420362, 223.405 } rm^3 +compflowStatistics, caprock: Phase mass: { 185.824, 216514 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 80.9086, 65077.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 104.916, 151437 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.58705, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 177.237, 216514 } kg +compflowStatistics, caprock: Dissolved component mass: { { 185.824, 0 }, { 195.332, 216315 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 39.2863 +compflowStatistics: Max component CFL number: 7.74695 +Time: 1.94e+08s, dt:1e+06s, Cycle: 1088 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.62e-03 ) ; + Line search @ 0.302: ( Rflow ) = ( 9.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.89e-03 ) ; + Line search @ 0.431: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.70e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.93e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.61e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 6.18e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00859768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.272662 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77823e+07, 1.78215e+07, 1.78581e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2838e+06, 5.35961e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.603 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.41121, 725.191 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3276.83, 702942 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.509, 213059 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2725.32, 489884 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.322, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3124.51, 702942 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3276.83, 0 }, { 1070.25, 701851 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77638e+07, 1.77763e+07, 1.7801e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26525e+06, 5.30252e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.825 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.423931, 223.401 } rm^3 +compflowStatistics, caprock: Phase mass: { 187.382, 216511 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 81.2579, 65077.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 106.124, 151433 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.50786, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 178.875, 216511 } kg +compflowStatistics, caprock: Dissolved component mass: { { 187.382, 0 }, { 196.273, 216310 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 35.6445 +compflowStatistics: Max component CFL number: 6.26058 +Time: 1.95e+08s, dt:1e+06s, Cycle: 1089 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.93e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.00e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.16e-03 ) ; + Line search @ 0.313: ( Rflow ) = ( 3.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.157: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.94e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.11e-03 ) ; + Line search @ 0.343: ( Rflow ) = ( 1.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.82e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.48e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-06 ) ; + Last LinSolve(iter,res) = ( 10, 9.11e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00827172 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.274211 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77809e+07, 1.782e+07, 1.78567e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.28231e+06, 5.35812e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.602 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.40341, 725.198 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3273.05, 702949 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.847, 213058 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2721.2, 489890 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.06, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3120.99, 702949 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3273.05, 0 }, { 1071.52, 701855 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77623e+07, 1.77749e+07, 1.77996e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26376e+06, 5.30103e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.825 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.427515, 223.397 } rm^3 +compflowStatistics, caprock: Phase mass: { 188.947, 216507 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 81.6095, 65077.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 107.338, 151429 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.56699, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 180.38, 216507 } kg +compflowStatistics, caprock: Dissolved component mass: { { 188.947, 0 }, { 197.218, 216306 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 26.0058 +compflowStatistics: Max component CFL number: 4.32287 +Time: 1.96e+08s, dt:1e+06s, Cycle: 1090 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.20e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; + Line search @ 0.338: ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.169: ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.65e-03 ) ; + Line search @ 0.413: ( Rflow ) = ( 9.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 7.49e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.49e-07 ) ; + Last LinSolve(iter,res) = ( 8, 5.20e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00860135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.253982 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77794e+07, 1.78185e+07, 1.78552e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.28088e+06, 5.35669e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.601 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.39544, 725.205 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3269.18, 702955 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.031, 213058 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2717.14, 489897 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.598, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3117.58, 702955 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3269.18, 0 }, { 1072.88, 701860 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77608e+07, 1.77734e+07, 1.77981e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26232e+06, 5.2996e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.824 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.431099, 223.393 } rm^3 +compflowStatistics, caprock: Phase mass: { 190.511, 216503 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 81.9588, 65077.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 108.552, 151425 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.54513, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 181.966, 216503 } kg +compflowStatistics, caprock: Dissolved component mass: { { 190.511, 0 }, { 198.167, 216301 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 18.9915 +compflowStatistics: Max component CFL number: 4.65014 +Time: 1.97e+08s, dt:1e+06s, Cycle: 1091 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.98e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.69e-03 ) ; + Line search @ 0.298: ( Rflow ) = ( 9.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e+00 ) ; + Last LinSolve(iter,res) = ( 6, 4.72e-03 ) ; + Line search @ 0.478: ( Rflow ) = ( 5.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.239: ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.120: ( Rflow ) = ( 8.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e+00 ) ; + Last LinSolve(iter,res) = ( 6, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.07e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.46e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.75e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 8.62e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.62e-06 ) ; + Last LinSolve(iter,res) = ( 8, 6.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00872519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.233114 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77779e+07, 1.7817e+07, 1.78537e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.27939e+06, 5.3552e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.599 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.38738, 725.212 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3265.26, 702961 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.191, 213057 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2713.07, 489904 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.222, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3114.04, 702961 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3265.26, 0 }, { 1074.28, 701865 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77593e+07, 1.77719e+07, 1.77966e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.26084e+06, 5.29811e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.824 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.434693, 223.389 } rm^3 +compflowStatistics, caprock: Phase mass: { 192.079, 216499 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 82.3087, 65077.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 109.77, 151422 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.5142, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 183.564, 216499 } kg +compflowStatistics, caprock: Dissolved component mass: { { 192.079, 0 }, { 199.114, 216296 } } kg +compflowStatistics: Max phase CFL number: 6.0357 +compflowStatistics: Max component CFL number: 4.42776 +Time: 1.98e+08s, dt:1e+06s, Cycle: 1092 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.03e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.389: ( Rflow ) = ( 7.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.194: ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.097: ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.07e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.07e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Line search @ 0.459: ( Rflow ) = ( 1.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.230: ( Rflow ) = ( 4.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.115: ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.057: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.39e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e+00 ) ; + Last LinSolve(iter,res) = ( 5, 9.10e-03 ) ; + Line search @ 0.485: ( Rflow ) = ( 1.47e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.243: ( Rflow ) = ( 6.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.121: ( Rflow ) = ( 3.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.061: ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.32e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.28e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 13, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 9, 6.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.39e-02 ) ; + Last LinSolve(iter,res) = ( 9, 5.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 3.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-03 ) ; + Last LinSolve(iter,res) = ( 9, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 12 + ( Rflow ) = ( 5.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-05 ) ; + Last LinSolve(iter,res) = ( 9, 7.28e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00858325 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.215353 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77764e+07, 1.78155e+07, 1.78522e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.27787e+06, 5.35368e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.598 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.37935, 725.219 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3261.36, 702967 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.406, 213057 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2708.96, 489911 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.202, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3110.16, 702967 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3261.36, 0 }, { 1075.65, 701870 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77578e+07, 1.77704e+07, 1.77951e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25933e+06, 5.29659e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.824 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.438294, 223.385 } rm^3 +compflowStatistics, caprock: Phase mass: { 193.649, 216495 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 82.6584, 65077.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 110.991, 151418 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.50784, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 185.142, 216495 } kg +compflowStatistics, caprock: Dissolved component mass: { { 193.649, 0 }, { 200.064, 216291 } } kg +compflowStatistics: Max phase CFL number: 5.24854 +compflowStatistics: Max component CFL number: 4.10437 +Time: 1.99e+08s, dt:1e+06s, Cycle: 1093 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.63e-03 ) ; + Line search @ 0.396: ( Rflow ) = ( 9.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.31e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.16e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00839141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.177491 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77749e+07, 1.7814e+07, 1.78507e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.27637e+06, 5.35218e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.597 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.37141, 725.226 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3257.51, 702973 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.697, 213056 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2704.82, 489917 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.068, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3106.45, 702973 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3257.51, 0 }, { 1076.97, 701875 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77563e+07, 1.77689e+07, 1.77936e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25782e+06, 5.29509e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.823 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.441909, 223.381 } rm^3 +compflowStatistics, caprock: Phase mass: { 195.226, 216491 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 83.0084, 65077.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 112.218, 151414 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.46827, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 186.758, 216491 } kg +compflowStatistics, caprock: Dissolved component mass: { { 195.226, 0 }, { 201.017, 216286 } } kg +compflowStatistics: Max phase CFL number: 4.94714 +compflowStatistics: Max component CFL number: 3.97124 +Time: 2e+08s, dt:1e+06s, Cycle: 1094 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; + Line search @ 0.406: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Line search @ 0.497: ( Rflow ) = ( 6.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 10, 1.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00820762 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.2201 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77735e+07, 1.78126e+07, 1.78493e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2749e+06, 5.35071e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.596 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.36358, 725.233 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3253.72, 702979 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.007, 213056 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2700.72, 489924 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.831, 0.00107404 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3102.89, 702979 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3253.72, 0 }, { 1078.22, 701880 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77549e+07, 1.77674e+07, 1.77922e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25634e+06, 5.29362e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.823 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.445537, 223.377 } rm^3 +compflowStatistics, caprock: Phase mass: { 196.809, 216487 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 83.3593, 65077 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 113.45, 151410 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.4652, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 188.344, 216487 } kg +compflowStatistics, caprock: Dissolved component mass: { { 196.809, 0 }, { 201.972, 216281 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.82058 +compflowStatistics: Max component CFL number: 3.71958 +Time: 2.01e+08s, dt:1e+06s, Cycle: 1095 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.75e-03 ) ; + Line search @ 0.253: ( Rflow ) = ( 9.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.68e-03 ) ; + Line search @ 0.348: ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.174: ( Rflow ) = ( 7.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.27e-03 ) ; + Line search @ 0.462: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.02e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-06 ) ; + Last LinSolve(iter,res) = ( 8, 6.31e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00816034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.253463 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7772e+07, 1.78112e+07, 1.78479e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.27347e+06, 5.34929e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.595 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.35575, 725.239 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3249.93, 702986 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.258, 213055 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2696.67, 489930 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.645, 0.001074 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3099.29, 702986 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3249.93, 0 }, { 1079.48, 701884 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77535e+07, 1.7766e+07, 1.77908e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25491e+06, 5.29219e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.823 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.449178, 223.373 } rm^3 +compflowStatistics, caprock: Phase mass: { 198.398, 216484 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 83.7121, 65077 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 114.686, 151407 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.46035, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 189.937, 216484 } kg +compflowStatistics, caprock: Dissolved component mass: { { 198.398, 0 }, { 202.926, 216277 } } kg +compflowStatistics: Max phase CFL number: 5.13022 +compflowStatistics: Max component CFL number: 3.26732 +Time: 2.02e+08s, dt:1e+06s, Cycle: 1096 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.45e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e+00 ) ; + Last LinSolve(iter,res) = ( 5, 9.12e-03 ) ; + Line search @ 0.305: ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.153: ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.076: ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.97e-03 ) ; + Line search @ 0.326: ( Rflow ) = ( 3.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.163: ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.45e-03 ) ; + Line search @ 0.390: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-01 ) ; + Last LinSolve(iter,res) = ( 8, 6.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-01 ) ; + Last LinSolve(iter,res) = ( 7, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.50e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.50e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.41e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0082792 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.216477 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77706e+07, 1.78098e+07, 1.78464e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.27205e+06, 5.34786e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.594 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.34784, 725.246 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3246.11, 702992 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.417, 213055 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2692.69, 489937 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.356, 0.00107394 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3095.75, 702992 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3246.11, 0 }, { 1080.76, 701889 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7752e+07, 1.77646e+07, 1.77893e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25348e+06, 5.29077e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.822 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.452826, 223.369 } rm^3 +compflowStatistics, caprock: Phase mass: { 199.988, 216480 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 84.0642, 65076.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 115.924, 151403 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.42534, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 191.563, 216480 } kg +compflowStatistics, caprock: Dissolved component mass: { { 199.988, 0 }, { 203.88, 216272 } } kg +compflowStatistics: Max phase CFL number: 5.95242 +compflowStatistics: Max component CFL number: 3.25328 +Time: 2.03e+08s, dt:1e+06s, Cycle: 1097 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e+00 ) ; + Last LinSolve(iter,res) = ( 7, 5.39e-03 ) ; + Line search @ 0.354: ( Rflow ) = ( 3.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.177: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.089: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e+00 ) ; + Last LinSolve(iter,res) = ( 7, 4.94e-03 ) ; + Line search @ 0.381: ( Rflow ) = ( 5.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.190: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.095: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.048: ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.75e-03 ) ; + Line search @ 0.428: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.79e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.96e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.11e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-05 ) ; + Last LinSolve(iter,res) = ( 9, 8.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00822205 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.204207 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77692e+07, 1.78083e+07, 1.7845e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2706e+06, 5.34641e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.593 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.33996, 725.253 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3242.3, 702998 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.613, 213054 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2688.68, 489944 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.217, 0.0010739 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3092.08, 702998 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3242.3, 0 }, { 1082.02, 701894 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77506e+07, 1.77631e+07, 1.77879e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.25204e+06, 5.28932e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.822 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.456483, 223.365 } rm^3 +compflowStatistics, caprock: Phase mass: { 201.583, 216476 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 84.4171, 65076.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 117.166, 151399 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.43198, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 193.151, 216476 } kg +compflowStatistics, caprock: Dissolved component mass: { { 201.583, 0 }, { 204.836, 216267 } } kg +compflowStatistics: Max phase CFL number: 7.00448 +compflowStatistics: Max component CFL number: 3.03217 +Time: 2.04e+08s, dt:1e+06s, Cycle: 1098 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.10e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.28e-03 ) ; + Line search @ 0.330: ( Rflow ) = ( 2.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.165: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.57e-03 ) ; + Line search @ 0.390: ( Rflow ) = ( 4.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.195: ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.097: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.049: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.53e-03 ) ; + Line search @ 0.411: ( Rflow ) = ( 9.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.24e-03 ) ; + Line search @ 0.482: ( Rflow ) = ( 8.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.90e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00824186 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.263493 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77677e+07, 1.78069e+07, 1.78435e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26916e+06, 5.34498e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.592 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.33206, 725.26 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3238.47, 703004 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.821, 213054 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2684.65, 489950 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.142, 0.00107386 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3088.33, 703004 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3238.47, 0 }, { 1083.29, 701899 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77492e+07, 1.77617e+07, 1.77864e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2506e+06, 5.28789e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.822 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.460148, 223.361 } rm^3 +compflowStatistics, caprock: Phase mass: { 203.181, 216472 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 84.7709, 65076.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 118.41, 151395 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.4562, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 194.725, 216472 } kg +compflowStatistics, caprock: Dissolved component mass: { { 203.181, 0 }, { 205.793, 216262 } } kg +compflowStatistics: Max phase CFL number: 7.91428 +compflowStatistics: Max component CFL number: 2.83216 +Time: 2.05e+08s, dt:1e+06s, Cycle: 1099 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.26e-03 ) ; + Line search @ 0.312: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.04e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-04 ) ; + Last LinSolve(iter,res) = ( 9, 5.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00821554 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.214996 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77663e+07, 1.78054e+07, 1.78421e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26772e+06, 5.34354e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.591 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.32414, 725.267 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3234.64, 703010 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.049, 213053 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2680.59, 489957 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.933, 0.00107381 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3084.71, 703010 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3234.64, 0 }, { 1084.56, 701904 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77477e+07, 1.77602e+07, 1.7785e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24916e+06, 5.28644e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.821 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.463823, 223.358 } rm^3 +compflowStatistics, caprock: Phase mass: { 204.783, 216468 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 85.1268, 65076.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 119.656, 151391 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.55144, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 196.231, 216468 } kg +compflowStatistics, caprock: Dissolved component mass: { { 204.783, 0 }, { 206.75, 216257 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 7.68436 +compflowStatistics: Max component CFL number: 2.77793 +Time: 2.06e+08s, dt:1e+06s, Cycle: 1100 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-01 ) ; + Last LinSolve(iter,res) = ( 7, 7.92e-03 ) ; + Line search @ 0.302: ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.151: ( Rflow ) = ( 1.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.076: ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.95e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.67e-03 ) ; + Line search @ 0.324: ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.162: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.26e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; + Line search @ 0.384: ( Rflow ) = ( 8.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 9.16e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.16e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00843949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.254817 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77648e+07, 1.78039e+07, 1.78406e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26628e+06, 5.34209e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.59 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.31609, 725.274 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3230.75, 703016 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.198, 213053 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2676.55, 489964 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.619, 0.00107377 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3081.13, 703016 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3230.75, 0 }, { 1085.9, 701909 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77462e+07, 1.77588e+07, 1.77835e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24772e+06, 5.285e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.821 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.467509, 223.353 } rm^3 +compflowStatistics, caprock: Phase mass: { 206.388, 216464 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 85.4841, 65076.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 120.904, 151388 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.52219, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 197.866, 216464 } kg +compflowStatistics, caprock: Dissolved component mass: { { 206.388, 0 }, { 207.699, 216252 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 7.46918 +compflowStatistics: Max component CFL number: 2.70079 +Time: 2.07e+08s, dt:1e+06s, Cycle: 1101 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; + Line search @ 0.347: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.35e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.54e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.68e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00844808 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.204507 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77633e+07, 1.78025e+07, 1.78391e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26479e+06, 5.34061e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.589 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.30802, 725.281 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3226.84, 703023 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.329, 213052 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2672.51, 489970 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.404, 0.00107374 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3077.44, 703023 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3226.84, 0 }, { 1087.24, 701914 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77448e+07, 1.77573e+07, 1.7782e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24624e+06, 5.28351e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.821 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.471205, 223.349 } rm^3 +compflowStatistics, caprock: Phase mass: { 207.998, 216460 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 85.8417, 65076.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 122.156, 151384 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.45007, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 199.548, 216460 } kg +compflowStatistics, caprock: Dissolved component mass: { { 207.998, 0 }, { 208.646, 216247 } } kg +compflowStatistics: Max phase CFL number: 6.60629 +compflowStatistics: Max component CFL number: 2.59894 +Time: 2.08e+08s, dt:1e+06s, Cycle: 1102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.95e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.88e-03 ) ; + Line search @ 0.385: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.70e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.10e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00820356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.188457 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77619e+07, 1.7801e+07, 1.78377e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2633e+06, 5.33912e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.588 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.3001, 725.288 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3223.02, 703029 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.594, 213052 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2668.42, 489977 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.433, 0.00107371 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3073.58, 703029 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3223.02, 0 }, { 1088.51, 701919 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77433e+07, 1.77558e+07, 1.77806e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24476e+06, 5.28203e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.82 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.474921, 223.345 } rm^3 +compflowStatistics, caprock: Phase mass: { 209.617, 216456 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 86.2027, 65076.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 123.415, 151380 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.42168, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 201.196, 216456 } kg +compflowStatistics, caprock: Dissolved component mass: { { 209.617, 0 }, { 209.589, 216242 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.93147 +compflowStatistics: Max component CFL number: 2.57217 +Time: 2.09e+08s, dt:1e+06s, Cycle: 1103 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.95e-03 ) ; + Line search @ 0.447: ( Rflow ) = ( 3.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.224: ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.77e-03 ) ; + Line search @ 0.481: ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0081896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.191649 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77604e+07, 1.77996e+07, 1.78363e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26188e+06, 5.33769e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.587 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.29213, 725.295 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3219.17, 703035 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.842, 213051 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2664.33, 489984 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.293, 0.00107367 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3069.88, 703035 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3219.17, 0 }, { 1089.79, 701923 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77419e+07, 1.77544e+07, 1.77792e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24332e+06, 5.2806e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.82 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.478654, 223.341 } rm^3 +compflowStatistics, caprock: Phase mass: { 211.243, 216452 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 86.5687, 65076.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 124.674, 151376 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.50785, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 202.735, 216452 } kg +compflowStatistics, caprock: Dissolved component mass: { { 211.243, 0 }, { 210.526, 216238 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.47976 +compflowStatistics: Max component CFL number: 2.53252 +Time: 2.1e+08s, dt:1e+06s, Cycle: 1104 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Line search @ 0.449: ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.224: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.91e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.91e-06 ) ; + Last LinSolve(iter,res) = ( 8, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00811033 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.193664 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7759e+07, 1.77982e+07, 1.78348e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.26044e+06, 5.33625e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.586 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.28418, 725.302 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3215.34, 703041 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.049, 213051 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2660.29, 489990 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.116, 0.00107363 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3066.22, 703041 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3215.34, 0 }, { 1091.07, 701928 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77404e+07, 1.7753e+07, 1.77777e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24188e+06, 5.27916e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.82 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.482413, 223.337 } rm^3 +compflowStatistics, caprock: Phase mass: { 212.881, 216448 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 86.9422, 65076.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 125.938, 151372 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.54129, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 204.339, 216448 } kg +compflowStatistics, caprock: Dissolved component mass: { { 212.881, 0 }, { 211.445, 216233 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.01096 +compflowStatistics: Max component CFL number: 2.44768 +Time: 2.11e+08s, dt:1e+06s, Cycle: 1105 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Line search @ 0.301: ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.30e-03 ) ; + Line search @ 0.481: ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.43e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.36e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0079696 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.259914 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77576e+07, 1.77968e+07, 1.78334e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.25901e+06, 5.33483e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.585 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.2763, 725.308 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3211.54, 703047 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.22, 213050 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2656.32, 489997 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.804, 0.00107361 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3062.74, 703047 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3211.54, 0 }, { 1092.31, 701933 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77391e+07, 1.77516e+07, 1.77763e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.24045e+06, 5.27773e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.819 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.486199, 223.333 } rm^3 +compflowStatistics, caprock: Phase mass: { 214.53, 216444 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 87.3224, 65076 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 127.208, 151368 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.52021, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 206.01, 216444 } kg +compflowStatistics, caprock: Dissolved component mass: { { 214.53, 0 }, { 212.352, 216228 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.44142 +compflowStatistics: Max component CFL number: 2.43203 +Time: 2.12e+08s, dt:1e+06s, Cycle: 1106 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Line search @ 0.301: ( Rflow ) = ( 9.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.55e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.38e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.75e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.02e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0078338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.226798 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77563e+07, 1.77954e+07, 1.78321e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.25762e+06, 5.33344e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.584 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.26848, 725.315 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3207.78, 703054 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.447, 213050 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2652.33, 490004 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.822, 0.00107357 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3058.96, 703054 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3207.78, 0 }, { 1093.52, 701938 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77377e+07, 1.77502e+07, 1.7775e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.23905e+06, 5.27634e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.819 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.490007, 223.329 } rm^3 +compflowStatistics, caprock: Phase mass: { 216.19, 216440 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 87.7069, 65076 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 128.483, 151364 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.50513, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 207.685, 216440 } kg +compflowStatistics, caprock: Dissolved component mass: { { 216.19, 0 }, { 213.248, 216223 } } kg +compflowStatistics: Max phase CFL number: 3.94821 +compflowStatistics: Max component CFL number: 2.37374 +Time: 2.13e+08s, dt:1e+06s, Cycle: 1107 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.19e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; + Line search @ 0.338: ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.169: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Line search @ 0.424: ( Rflow ) = ( 4.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.212: ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.106: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.27e-03 ) ; + Line search @ 0.491: ( Rflow ) = ( 4.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.245: ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.123: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.061: ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.89e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.48e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.10e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00788627 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.214288 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77549e+07, 1.7794e+07, 1.78307e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.25625e+06, 5.33207e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.583 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.26059, 725.322 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3203.98, 703060 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.65, 213049 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2648.33, 490010 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.671, 0.00107355 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3055.31, 703060 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3203.98, 0 }, { 1094.76, 701943 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77363e+07, 1.77488e+07, 1.77736e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.23768e+06, 5.27498e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.819 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.493834, 223.325 } rm^3 +compflowStatistics, caprock: Phase mass: { 217.857, 216436 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 88.0967, 65075.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 129.76, 151360 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.54833, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 209.309, 216436 } kg +compflowStatistics, caprock: Dissolved component mass: { { 217.857, 0 }, { 214.132, 216218 } } kg +compflowStatistics: Max phase CFL number: 4.09107 +compflowStatistics: Max component CFL number: 2.29856 +Time: 2.14e+08s, dt:1e+06s, Cycle: 1108 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Line search @ 0.316: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.03e-03 ) ; + Line search @ 0.439: ( Rflow ) = ( 8.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.80e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.80e-06 ) ; + Last LinSolve(iter,res) = ( 7, 3.90e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00797424 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.219747 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77535e+07, 1.77926e+07, 1.78293e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.25487e+06, 5.33069e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.582 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.25264, 725.329 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3200.16, 703066 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.812, 213049 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2644.34, 490017 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.484, 0.00107352 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3051.67, 703066 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3200.16, 0 }, { 1096.04, 701948 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77349e+07, 1.77474e+07, 1.77722e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2363e+06, 5.27359e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.818 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.497678, 223.321 } rm^3 +compflowStatistics, caprock: Phase mass: { 219.531, 216432 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 88.4926, 65075.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 131.038, 151356 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.65505, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 210.876, 216432 } kg +compflowStatistics, caprock: Dissolved component mass: { { 219.531, 0 }, { 215.006, 216213 } } kg +compflowStatistics: Max phase CFL number: 3.91617 +compflowStatistics: Max component CFL number: 2.25194 +Time: 2.15e+08s, dt:1e+06s, Cycle: 1109 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.50e-03 ) ; + Line search @ 0.248: ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; + Line search @ 0.346: ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.91e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00798847 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.258496 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77521e+07, 1.77912e+07, 1.78279e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.25347e+06, 5.32929e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.581 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.24467, 725.336 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3196.32, 703072 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.944, 213049 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2640.38, 490024 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.364, 0.00107349 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3047.96, 703072 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3196.32, 0 }, { 1097.33, 701953 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77335e+07, 1.7746e+07, 1.77708e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.23491e+06, 5.2722e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.818 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.501539, 223.317 } rm^3 +compflowStatistics, caprock: Phase mass: { 221.212, 216428 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 88.8938, 65075.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 132.319, 151352 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.7822, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 212.43, 216428 } kg +compflowStatistics, caprock: Dissolved component mass: { { 221.212, 0 }, { 215.868, 216208 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.51261 +compflowStatistics: Max component CFL number: 2.16167 +Time: 2.16e+08s, dt:1e+06s, Cycle: 1110 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; + Last LinSolve(iter,res) = ( 4, 1.00e-02 ) ; + Line search @ 0.290: ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e+00 ) ; + Last LinSolve(iter,res) = ( 5, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.08e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.35e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-04 ) ; + Last LinSolve(iter,res) = ( 7, 1.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00783158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.204449 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77507e+07, 1.77899e+07, 1.78265e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.25207e+06, 5.32789e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.58 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.23675, 725.343 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3192.52, 703079 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.103, 213048 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2636.42, 490031 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.16, 0.00107346 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3044.36, 703079 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3192.52, 0 }, { 1098.59, 701958 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77321e+07, 1.77446e+07, 1.77694e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.23351e+06, 5.2708e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.818 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.505424, 223.312 } rm^3 +compflowStatistics, caprock: Phase mass: { 222.904, 216424 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 89.301, 65075.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 133.603, 151348 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.81037, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 214.094, 216424 } kg +compflowStatistics, caprock: Dissolved component mass: { { 222.904, 0 }, { 216.719, 216203 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.47139 +compflowStatistics: Max component CFL number: 2.15036 +Time: 2.17e+08s, dt:1e+06s, Cycle: 1111 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.25e-03 ) ; + Line search @ 0.353: ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.10e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.78e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.30e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-06 ) ; + Last LinSolve(iter,res) = ( 9, 9.97e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0075828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.245768 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77494e+07, 1.77886e+07, 1.78252e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2507e+06, 5.32652e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.579 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.22901, 725.35 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3188.81, 703085 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.35, 213048 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2632.46, 490037 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.173, 0.00107343 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3040.64, 703085 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3188.81, 0 }, { 1099.75, 701963 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77308e+07, 1.77433e+07, 1.77681e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.23213e+06, 5.26943e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.818 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.509336, 223.308 } rm^3 +compflowStatistics, caprock: Phase mass: { 224.609, 216420 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 89.715, 65075.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 134.894, 151344 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.88652, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 215.722, 216420 } kg +compflowStatistics, caprock: Dissolved component mass: { { 224.609, 0 }, { 217.56, 216198 } } kg +compflowStatistics: Max phase CFL number: 2.89062 +compflowStatistics: Max component CFL number: 2.13994 +Time: 2.18e+08s, dt:1e+06s, Cycle: 1112 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; + Line search @ 0.337: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.38e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.41e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.41e-01 ) ; + Last LinSolve(iter,res) = ( 6, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.75e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-06 ) ; + Last LinSolve(iter,res) = ( 8, 4.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00736831 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.20899 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77481e+07, 1.77873e+07, 1.7824e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2494e+06, 5.32522e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.578 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.22135, 725.356 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3185.14, 703091 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.665, 213047 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2628.48, 490044 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.313, 0.0010734 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3036.83, 703091 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3185.14, 0 }, { 1100.87, 701968 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77295e+07, 1.77421e+07, 1.77669e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.23082e+06, 5.26813e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.817 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.513261, 223.304 } rm^3 +compflowStatistics, caprock: Phase mass: { 226.319, 216416 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 90.1298, 65075.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 136.189, 151340 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.91294, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 217.406, 216416 } kg +compflowStatistics, caprock: Dissolved component mass: { { 226.319, 0 }, { 218.401, 216193 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.70585 +compflowStatistics: Max component CFL number: 2.10249 +Time: 2.19e+08s, dt:1e+06s, Cycle: 1113 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.38e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; + Line search @ 0.440: ( Rflow ) = ( 4.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.220: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.110: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e+00 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; + Line search @ 0.495: ( Rflow ) = ( 5.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.247: ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.124: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.53e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00718221 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.188216 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77469e+07, 1.7786e+07, 1.78227e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24813e+06, 5.32395e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.577 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.21375, 725.363 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3181.51, 703097 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.97, 213047 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2624.54, 490050 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.217, 0.00107337 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3033.29, 703097 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3181.51, 0 }, { 1101.95, 701973 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77283e+07, 1.77408e+07, 1.77656e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22954e+06, 5.26686e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.817 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.517208, 223.3 } rm^3 +compflowStatistics, caprock: Phase mass: { 228.04, 216412 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 90.5486, 65075.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 137.491, 151336 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.91324, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 219.126, 216412 } kg +compflowStatistics, caprock: Dissolved component mass: { { 228.04, 0 }, { 219.232, 216188 } } kg +compflowStatistics: Max phase CFL number: 5.74303 +compflowStatistics: Max component CFL number: 2.64723 +Time: 2.2e+08s, dt:1e+06s, Cycle: 1114 +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.39e-03 ) ; + Line search @ 0.384: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.21e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.91e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00700601 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.1907 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77457e+07, 1.77848e+07, 1.78215e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24689e+06, 5.32271e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.576 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.20621, 725.37 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3177.91, 703103 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.239, 213046 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2620.67, 490057 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.874, 0.00107335 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3030.04, 703103 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3177.91, 0 }, { 1103, 701978 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77271e+07, 1.77396e+07, 1.77644e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22829e+06, 5.26561e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.817 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.521184, 223.296 } rm^3 +compflowStatistics, caprock: Phase mass: { 229.773, 216408 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 90.9767, 65075.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 138.796, 151332 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.02972, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 220.743, 216408 } kg +compflowStatistics, caprock: Dissolved component mass: { { 229.773, 0 }, { 220.046, 216183 } } kg +compflowStatistics: Max phase CFL number: 5.24237 +compflowStatistics: Max component CFL number: 2.99762 +Time: 2.21e+08s, dt:1e+06s, Cycle: 1115 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.389: ( Rflow ) = ( 8.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.95e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.71e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00687213 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.237245 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77445e+07, 1.77836e+07, 1.78203e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24568e+06, 5.3215e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.575 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.19869, 725.376 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3174.33, 703109 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.408, 213046 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2616.92, 490063 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.682, 0.00107332 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3026.64, 703109 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3174.33, 0 }, { 1104.05, 701983 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77259e+07, 1.77384e+07, 1.77632e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22707e+06, 5.2644e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.816 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.525188, 223.291 } rm^3 +compflowStatistics, caprock: Phase mass: { 231.518, 216403 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 91.4144, 65075.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 140.104, 151328 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.21836, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 222.3, 216403 } kg +compflowStatistics, caprock: Dissolved component mass: { { 231.518, 0 }, { 220.842, 216178 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.30915 +compflowStatistics: Max component CFL number: 2.85866 +Time: 2.22e+08s, dt:1e+06s, Cycle: 1116 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.15e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.10e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.31e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00680395 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.183003 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77433e+07, 1.77824e+07, 1.78191e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24448e+06, 5.3203e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.574 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.19116, 725.383 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3170.73, 703115 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.558, 213046 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2613.18, 490069 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.452, 0.0010733 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3023.28, 703115 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3170.73, 0 }, { 1105.1, 701988 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77247e+07, 1.77372e+07, 1.7762e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22587e+06, 5.2632e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.816 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.529206, 223.287 } rm^3 +compflowStatistics, caprock: Phase mass: { 233.27, 216399 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 91.853, 65075.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 141.417, 151324 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.21799, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 224.052, 216399 } kg +compflowStatistics, caprock: Dissolved component mass: { { 233.27, 0 }, { 221.63, 216173 } } kg +compflowStatistics: Max phase CFL number: 5.37435 +compflowStatistics: Max component CFL number: 2.6569 +Time: 2.23e+08s, dt:1e+06s, Cycle: 1117 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e+00 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.420: ( Rflow ) = ( 9.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.210: ( Rflow ) = ( 4.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.105: ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.052: ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.66e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Line search @ 0.462: ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.231: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.51e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.22e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00692415 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.191833 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77421e+07, 1.77812e+07, 1.78179e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24328e+06, 5.3191e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.573 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.18356, 725.39 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3167.11, 703121 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.632, 213045 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2609.48, 490076 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.185, 0.00107327 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3019.92, 703121 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3167.11, 0 }, { 1106.19, 701993 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77235e+07, 1.7736e+07, 1.77608e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22467e+06, 5.26201e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.816 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.533239, 223.283 } rm^3 +compflowStatistics, caprock: Phase mass: { 235.027, 216395 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 92.2945, 65075.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 142.733, 151320 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.22158, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 225.806, 216395 } kg +compflowStatistics, caprock: Dissolved component mass: { { 235.027, 0 }, { 222.409, 216168 } } kg +compflowStatistics: Max phase CFL number: 5.09816 +compflowStatistics: Max component CFL number: 2.62102 +Time: 2.24e+08s, dt:1e+06s, Cycle: 1118 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.44e-03 ) ; + Line search @ 0.398: ( Rflow ) = ( 9.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.88e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.60e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.60e-06 ) ; + Last LinSolve(iter,res) = ( 8, 2.22e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00693309 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.245003 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77408e+07, 1.778e+07, 1.78167e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24207e+06, 5.31789e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.573 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.17593, 725.397 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3163.47, 703127 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.708, 213045 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2605.76, 490082 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.126, 0.00107325 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3016.34, 703127 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3163.47, 0 }, { 1107.29, 701998 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77222e+07, 1.77347e+07, 1.77596e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22346e+06, 5.26079e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.816 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.537281, 223.278 } rm^3 +compflowStatistics, caprock: Phase mass: { 236.788, 216391 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 92.7384, 65075 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 144.05, 151316 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.36386, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 227.425, 216391 } kg +compflowStatistics, caprock: Dissolved component mass: { { 236.788, 0 }, { 223.183, 216163 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.98863 +compflowStatistics: Max component CFL number: 2.44052 +Time: 2.25e+08s, dt:1e+06s, Cycle: 1119 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; + Line search @ 0.295: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.51e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.38e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.38e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00683594 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.203502 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77396e+07, 1.77788e+07, 1.78155e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.24085e+06, 5.31667e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.572 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.16835, 725.403 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3159.85, 703133 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.834, 213044 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2602.02, 490089 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.912, 0.00107323 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3012.94, 703133 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3159.85, 0 }, { 1108.37, 702003 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7721e+07, 1.77335e+07, 1.77584e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22224e+06, 5.25957e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.815 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.541335, 223.274 } rm^3 +compflowStatistics, caprock: Phase mass: { 238.555, 216387 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 93.1841, 65074.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 145.37, 151312 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.49599, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 229.059, 216387 } kg +compflowStatistics, caprock: Dissolved component mass: { { 238.555, 0 }, { 223.956, 216158 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.94188 +compflowStatistics: Max component CFL number: 1.97497 +Time: 2.26e+08s, dt:1e+06s, Cycle: 1120 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.86e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e+00 ) ; + Last LinSolve(iter,res) = ( 5, 9.33e-03 ) ; + Line search @ 0.322: ( Rflow ) = ( 7.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.161: ( Rflow ) = ( 2.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.080: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Line search @ 0.237: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.71e-03 ) ; + Line search @ 0.399: ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.199: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00677454 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.292475 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77385e+07, 1.77776e+07, 1.78143e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23964e+06, 5.31546e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.571 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.16079, 725.41 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3156.26, 703139 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.005, 213044 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2598.25, 490095 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.869, 0.0010732 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3009.39, 703139 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3156.26, 0 }, { 1109.43, 702008 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77198e+07, 1.77323e+07, 1.77572e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.22103e+06, 5.25836e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.815 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.545404, 223.27 } rm^3 +compflowStatistics, caprock: Phase mass: { 240.327, 216382 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 93.6333, 65074.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 146.694, 151308 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.60222, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 230.725, 216382 } kg +compflowStatistics, caprock: Dissolved component mass: { { 240.327, 0 }, { 224.722, 216153 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.6432 +compflowStatistics: Max component CFL number: 1.81414 +Time: 2.27e+08s, dt:1e+06s, Cycle: 1121 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.50e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.14e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.21e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.61e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00681074 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.17798 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77373e+07, 1.77764e+07, 1.78131e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23845e+06, 5.31427e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.57 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.15321, 725.417 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3152.65, 703146 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.186, 213044 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2594.46, 490102 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.886, 0.00107318 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3005.76, 703146 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3152.65, 0 }, { 1110.5, 702013 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77186e+07, 1.77312e+07, 1.7756e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21984e+06, 5.25717e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.815 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.549496, 223.265 } rm^3 +compflowStatistics, caprock: Phase mass: { 242.11, 216378 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 94.0886, 65074.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 148.022, 151303 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.71185, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 232.398, 216378 } kg +compflowStatistics, caprock: Dissolved component mass: { { 242.11, 0 }, { 225.473, 216148 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.61636 +compflowStatistics: Max component CFL number: 1.7548 +Time: 2.28e+08s, dt:1e+06s, Cycle: 1122 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Line search @ 0.294: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.46e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0066684 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.23141 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77361e+07, 1.77753e+07, 1.78119e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23727e+06, 5.31309e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.569 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.14567, 725.423 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3149.07, 703152 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.406, 213043 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2590.66, 490108 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.759, 0.00107316 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 3002.31, 703152 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3149.07, 0 }, { 1111.55, 702018 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77175e+07, 1.773e+07, 1.77548e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21865e+06, 5.25599e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.815 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.553603, 223.261 } rm^3 +compflowStatistics, caprock: Phase mass: { 243.899, 216374 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 94.546, 65074.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 149.353, 151299 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.75151, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 234.148, 216374 } kg +compflowStatistics, caprock: Dissolved component mass: { { 243.899, 0 }, { 226.218, 216143 } } kg +compflowStatistics: Max phase CFL number: 3.45909 +compflowStatistics: Max component CFL number: 1.70405 +Time: 2.29e+08s, dt:1e+06s, Cycle: 1123 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.56e-03 ) ; + Line search @ 0.303: ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.22e-03 ) ; + Line search @ 0.494: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.25e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00661037 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.221444 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77349e+07, 1.77741e+07, 1.78108e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2361e+06, 5.31192e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.568 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.13815, 725.43 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3145.49, 703158 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.584, 213043 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2586.91, 490115 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.576, 0.00107314 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2998.92, 703158 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3145.49, 0 }, { 1112.58, 702023 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77163e+07, 1.77288e+07, 1.77537e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21747e+06, 5.25482e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.814 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.557714, 223.257 } rm^3 +compflowStatistics, caprock: Phase mass: { 245.69, 216370 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 95.0047, 65074.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 150.686, 151295 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.98599, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 235.704, 216370 } kg +compflowStatistics, caprock: Dissolved component mass: { { 245.69, 0 }, { 226.966, 216138 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.46049 +compflowStatistics: Max component CFL number: 1.62598 +Time: 2.3e+08s, dt:1e+06s, Cycle: 1124 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.342: ( Rflow ) = ( 4.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.171: ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.31e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.97e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00656949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.180719 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77338e+07, 1.77729e+07, 1.78096e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23493e+06, 5.31075e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.567 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.13066, 725.437 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3141.93, 703164 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.685, 213042 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2583.25, 490121 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.221, 0.00107312 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2995.71, 703164 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3141.93, 0 }, { 1113.6, 702028 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77152e+07, 1.77277e+07, 1.77525e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21631e+06, 5.25366e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.814 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.561833, 223.252 } rm^3 +compflowStatistics, caprock: Phase mass: { 247.485, 216365 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 95.4636, 65074.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 152.021, 151291 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.1217, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 237.363, 216365 } kg +compflowStatistics, caprock: Dissolved component mass: { { 247.485, 0 }, { 227.713, 216133 } } kg +compflowStatistics: Max phase CFL number: 3.33689 +compflowStatistics: Max component CFL number: 1.58288 +Time: 2.31e+08s, dt:1e+06s, Cycle: 1125 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.29e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.13e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.38e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.38e-07 ) ; + Last LinSolve(iter,res) = ( 9, 1.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00656945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.171401 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77326e+07, 1.77718e+07, 1.78085e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23378e+06, 5.3096e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.567 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.12315, 725.443 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3138.36, 703170 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.778, 213042 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2579.59, 490128 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.043, 0.0010731 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2992.32, 703170 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3138.36, 0 }, { 1114.63, 702033 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7714e+07, 1.77265e+07, 1.77514e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21516e+06, 5.25251e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.814 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.565961, 223.248 } rm^3 +compflowStatistics, caprock: Phase mass: { 249.283, 216361 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 95.9213, 65074.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 153.361, 151287 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.1651, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 239.117, 216361 } kg +compflowStatistics, caprock: Dissolved component mass: { { 249.283, 0 }, { 228.458, 216128 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.63317 +compflowStatistics: Max component CFL number: 1.51603 +Time: 2.32e+08s, dt:1e+06s, Cycle: 1126 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.17e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.07e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.07e-06 ) ; + Last LinSolve(iter,res) = ( 9, 1.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00645104 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.248414 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77315e+07, 1.77707e+07, 1.78073e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23263e+06, 5.30845e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.566 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.11569, 725.45 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3134.83, 703176 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.889, 213042 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2575.94, 490134 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.028, 0.00107308 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2988.8, 703176 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3134.83, 0 }, { 1115.62, 702038 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77129e+07, 1.77254e+07, 1.77502e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21401e+06, 5.25135e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.814 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.570111, 223.243 } rm^3 +compflowStatistics, caprock: Phase mass: { 251.09, 216357 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 96.3846, 65074.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 154.706, 151282 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.2199, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 240.87, 216357 } kg +compflowStatistics, caprock: Dissolved component mass: { { 251.09, 0 }, { 229.19, 216123 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.50517 +compflowStatistics: Max component CFL number: 2.05765 +Time: 2.33e+08s, dt:1e+06s, Cycle: 1127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.99e-03 ) ; + Line search @ 0.386: ( Rflow ) = ( 7.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.10e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.96e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.19e-04 ) ; + Last LinSolve(iter,res) = ( 9, 8.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00644966 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.184613 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77304e+07, 1.77695e+07, 1.78062e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2315e+06, 5.30732e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.565 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.1082, 725.457 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3131.28, 703182 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.017, 213041 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2572.26, 490141 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.931, 0.00107306 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2985.35, 703182 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3131.28, 0 }, { 1116.64, 702043 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77117e+07, 1.77242e+07, 1.77491e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21287e+06, 5.25022e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.813 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.574275, 223.239 } rm^3 +compflowStatistics, caprock: Phase mass: { 252.904, 216352 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 96.8512, 65074.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 156.053, 151278 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.3761, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 242.528, 216352 } kg +compflowStatistics, caprock: Dissolved component mass: { { 252.904, 0 }, { 229.914, 216118 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.85874 +compflowStatistics: Max component CFL number: 2.01906 +Time: 2.34e+08s, dt:1e+06s, Cycle: 1128 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Line search @ 0.422: ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.211: ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.30e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.33e-03 ) ; + Line search @ 0.495: ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.68e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.11e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.11e-04 ) ; + Last LinSolve(iter,res) = ( 7, 9.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00646531 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.210955 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77292e+07, 1.77684e+07, 1.78051e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.23037e+06, 5.30619e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.564 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.1007, 725.463 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3127.72, 703188 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.132, 213041 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2568.58, 490147 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.845, 0.00107304 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2981.87, 703188 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3127.72, 0 }, { 1117.66, 702048 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77106e+07, 1.77231e+07, 1.7748e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.21174e+06, 5.24909e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.813 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.578449, 223.235 } rm^3 +compflowStatistics, caprock: Phase mass: { 254.721, 216348 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 97.3186, 65074.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 157.403, 151274 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.4588, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 244.263, 216348 } kg +compflowStatistics, caprock: Dissolved component mass: { { 254.721, 0 }, { 230.634, 216113 } } kg +compflowStatistics: Max phase CFL number: 3.95626 +compflowStatistics: Max component CFL number: 1.95949 +Time: 2.35e+08s, dt:1e+06s, Cycle: 1129 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; + Line search @ 0.383: ( Rflow ) = ( 7.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.36e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00660169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.246944 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77281e+07, 1.77672e+07, 1.78039e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22923e+06, 5.30505e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.563 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.09312, 725.47 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3124.12, 703194 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.244, 213041 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2564.88, 490154 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.595, 0.00107302 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2978.53, 703194 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3124.12, 0 }, { 1118.72, 702053 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77095e+07, 1.7722e+07, 1.77468e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2106e+06, 5.24795e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.813 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.582633, 223.23 } rm^3 +compflowStatistics, caprock: Phase mass: { 256.543, 216344 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 97.7891, 65074.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 158.754, 151270 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.6255, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 245.917, 216344 } kg +compflowStatistics, caprock: Dissolved component mass: { { 256.543, 0 }, { 231.346, 216108 } } kg +compflowStatistics: Max phase CFL number: 4.90352 +compflowStatistics: Max component CFL number: 2.33029 +Time: 2.36e+08s, dt:1e+06s, Cycle: 1130 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.98e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e-01 ) ; + Last LinSolve(iter,res) = ( 7, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.30e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.30e-04 ) ; + Last LinSolve(iter,res) = ( 12, 4.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00654267 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.224535 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77269e+07, 1.77661e+07, 1.78027e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22807e+06, 5.3039e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.562 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.08555, 725.477 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3120.53, 703200 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.355, 213040 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2561.18, 490160 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.366, 0.00107301 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2975.17, 703200 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3120.53, 0 }, { 1119.78, 702058 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77083e+07, 1.77208e+07, 1.77456e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.20945e+06, 5.24679e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.813 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.586834, 223.226 } rm^3 +compflowStatistics, caprock: Phase mass: { 258.371, 216339 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 98.2645, 65074.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 160.107, 151265 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.7762, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 247.595, 216339 } kg +compflowStatistics, caprock: Dissolved component mass: { { 258.371, 0 }, { 232.049, 216103 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.93179 +compflowStatistics: Max component CFL number: 2.36094 +Time: 2.37e+08s, dt:1e+06s, Cycle: 1131 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.11e-01 ) ; + Last LinSolve(iter,res) = ( 11, 8.88e-03 ) ; + Line search @ 0.356: ( Rflow ) = ( 3.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.178: ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.089: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e+00 ) ; + Last LinSolve(iter,res) = ( 8, 7.43e-03 ) ; + Line search @ 0.393: ( Rflow ) = ( 5.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.197: ( Rflow ) = ( 2.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.098: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.049: ( Rflow ) = ( 1.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e+00 ) ; + Last LinSolve(iter,res) = ( 8, 8.30e-03 ) ; + Line search @ 0.429: ( Rflow ) = ( 6.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.215: ( Rflow ) = ( 3.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.107: ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.054: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 8, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 10, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.30e-04 ) ; + Last LinSolve(iter,res) = ( 8, 9.59e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00654852 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.197097 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77258e+07, 1.77649e+07, 1.78016e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22692e+06, 5.30275e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.562 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.07797, 725.484 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3116.94, 703207 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.451, 213040 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2557.49, 490167 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.311, 0.00107299 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2971.63, 703207 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3116.94, 0 }, { 1120.84, 702063 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77072e+07, 1.77197e+07, 1.77445e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2083e+06, 5.24565e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.812 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.591044, 223.221 } rm^3 +compflowStatistics, caprock: Phase mass: { 260.204, 216335 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 98.7405, 65074 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 161.463, 151261 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8434, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 249.36, 216335 } kg +compflowStatistics, caprock: Dissolved component mass: { { 260.204, 0 }, { 232.747, 216098 } } kg +compflowStatistics: Max phase CFL number: 2.67697 +compflowStatistics: Max component CFL number: 2.15928 +Time: 2.38e+08s, dt:1e+06s, Cycle: 1132 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.47e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.47e+00 ) ; + Last LinSolve(iter,res) = ( 9, 3.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.46e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e+00 ) ; + Last LinSolve(iter,res) = ( 7, 9.83e-03 ) ; + Line search @ 0.437: ( Rflow ) = ( 7.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.219: ( Rflow ) = ( 3.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.109: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.055: ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e+00 ) ; + Last LinSolve(iter,res) = ( 7, 6.51e-03 ) ; + Line search @ 0.456: ( Rflow ) = ( 8.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.228: ( Rflow ) = ( 3.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.114: ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.057: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.45e-03 ) ; + Line search @ 0.488: ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.244: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.52e-01 ) ; + Last LinSolve(iter,res) = ( 6, 7.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-01 ) ; + Last LinSolve(iter,res) = ( 6, 6.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 1.32e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-04 ) ; + Last LinSolve(iter,res) = ( 8, 7.79e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00656431 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.190257 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77246e+07, 1.77638e+07, 1.78004e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22577e+06, 5.3016e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.561 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.07038, 725.49 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3113.34, 703213 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.581, 213039 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2553.76, 490173 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.508, 0.00107297 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2967.83, 703213 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3113.34, 0 }, { 1121.9, 702068 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7706e+07, 1.77185e+07, 1.77433e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.20715e+06, 5.2445e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.812 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.595256, 223.217 } rm^3 +compflowStatistics, caprock: Phase mass: { 262.036, 216331 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 99.2124, 65074 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 162.824, 151257 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9303, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 251.106, 216331 } kg +compflowStatistics, caprock: Dissolved component mass: { { 262.036, 0 }, { 233.449, 216093 } } kg +compflowStatistics: Max phase CFL number: 4.12993 +compflowStatistics: Max component CFL number: 2.11774 +Time: 2.39e+08s, dt:1e+06s, Cycle: 1133 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.71e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 7, 4.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.11e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.11e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.18e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00651218 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.174014 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77235e+07, 1.77626e+07, 1.77993e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22462e+06, 5.30044e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.56 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.06281, 725.497 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3109.75, 703219 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.741, 213039 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2550.01, 490180 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.491, 0.00107295 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2964.26, 703219 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3109.75, 0 }, { 1122.96, 702074 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77049e+07, 1.77174e+07, 1.77422e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.206e+06, 5.24334e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.812 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.599479, 223.212 } rm^3 +compflowStatistics, caprock: Phase mass: { 263.874, 216326 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 99.6865, 65073.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 164.188, 151252 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.0585, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 252.816, 216326 } kg +compflowStatistics, caprock: Dissolved component mass: { { 263.874, 0 }, { 234.145, 216087 } } kg +compflowStatistics: Max phase CFL number: 5.38031 +compflowStatistics: Max component CFL number: 2.28618 +Time: 2.4e+08s, dt:1e+06s, Cycle: 1134 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Line search @ 0.351: ( Rflow ) = ( 6.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.49e-03 ) ; + Line search @ 0.499: ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0063103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.265926 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77224e+07, 1.77616e+07, 1.77982e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22348e+06, 5.2993e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.559 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.05539, 725.504 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3106.25, 703225 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.958, 213039 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2546.29, 490186 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.722, 0.00107294 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2960.53, 703225 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3106.25, 0 }, { 1123.92, 702079 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77038e+07, 1.77163e+07, 1.77411e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.20485e+06, 5.2422e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.812 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.603716, 223.208 } rm^3 +compflowStatistics, caprock: Phase mass: { 265.719, 216322 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 100.163, 65073.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 165.556, 151248 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.2307, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 254.488, 216322 } kg +compflowStatistics, caprock: Dissolved component mass: { { 265.719, 0 }, { 234.842, 216082 } } kg +compflowStatistics: Max phase CFL number: 5.3033 +compflowStatistics: Max component CFL number: 2.23375 +Time: 2.41e+08s, dt:1e+06s, Cycle: 1135 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Line search @ 0.308: ( Rflow ) = ( 8.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.69e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.49e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.38e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.27e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 2.87e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.87e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.97e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0061894 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.178128 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77213e+07, 1.77605e+07, 1.77971e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2224e+06, 5.29822e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.558 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.04799, 725.51 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3102.75, 703231 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.167, 213038 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2542.58, 490193 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.006, 0.00107292 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2956.75, 703231 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3102.75, 0 }, { 1124.88, 702084 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77027e+07, 1.77152e+07, 1.774e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.20376e+06, 5.24112e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.811 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.607965, 223.203 } rm^3 +compflowStatistics, caprock: Phase mass: { 267.568, 216318 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 100.641, 65073.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 166.927, 151244 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.3636, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 256.205, 216318 } kg +compflowStatistics, caprock: Dissolved component mass: { { 267.568, 0 }, { 235.534, 216077 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.99318 +compflowStatistics: Max component CFL number: 1.93582 +Time: 2.42e+08s, dt:1e+06s, Cycle: 1136 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.95e-03 ) ; + Line search @ 0.498: ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 7, 6.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.77e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00619356 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.185721 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77202e+07, 1.77594e+07, 1.77961e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22132e+06, 5.29714e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.558 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.04056, 725.517 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3099.24, 703237 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.342, 213038 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2538.9, 490199 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.056, 0.00107291 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2953.19, 703237 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3099.24, 0 }, { 1125.84, 702089 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77016e+07, 1.77141e+07, 1.7739e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.20268e+06, 5.24004e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.811 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.612218, 223.199 } rm^3 +compflowStatistics, caprock: Phase mass: { 269.42, 216313 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 101.119, 65073.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 168.301, 151240 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.5556, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 257.864, 216313 } kg +compflowStatistics, caprock: Dissolved component mass: { { 269.42, 0 }, { 236.225, 216072 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.51552 +compflowStatistics: Max component CFL number: 1.87898 +Time: 2.43e+08s, dt:1e+06s, Cycle: 1137 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.10e-03 ) ; + Line search @ 0.385: ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.193: ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.75e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.53e-03 ) ; + Line search @ 0.462: ( Rflow ) = ( 6.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.231: ( Rflow ) = ( 2.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.115: ( Rflow ) = ( 7.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 5.08e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.08e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00619863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.219829 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77192e+07, 1.77583e+07, 1.7795e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.22023e+06, 5.29606e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.557 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.03312, 725.524 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3095.73, 703243 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.48, 213038 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2535.25, 490205 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.229, 0.00107289 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2949.5, 703243 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3095.73, 0 }, { 1126.81, 702094 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.77005e+07, 1.7713e+07, 1.77379e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.2016e+06, 5.23896e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.811 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.616477, 223.194 } rm^3 +compflowStatistics, caprock: Phase mass: { 271.273, 216309 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 101.595, 65073.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 169.677, 151235 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.61, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 259.663, 216309 } kg +compflowStatistics, caprock: Dissolved component mass: { { 271.273, 0 }, { 236.916, 216067 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.81393 +compflowStatistics: Max component CFL number: 2.01271 +Time: 2.44e+08s, dt:1e+06s, Cycle: 1138 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.18e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Line search @ 0.319: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.25e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e+00 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.57e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 9 + ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 10 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 11 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.33e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00619698 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.200651 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77181e+07, 1.77572e+07, 1.77939e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21915e+06, 5.29498e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.556 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.02569, 725.53 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3092.22, 703249 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.631, 213037 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2531.59, 490212 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.593, 0.00107288 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2945.63, 703249 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3092.22, 0 }, { 1127.77, 702099 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76994e+07, 1.77119e+07, 1.77368e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.20051e+06, 5.23787e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.811 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.620739, 223.19 } rm^3 +compflowStatistics, caprock: Phase mass: { 273.127, 216304 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 102.069, 65073.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 171.058, 151231 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.6952, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 261.432, 216304 } kg +compflowStatistics, caprock: Dissolved component mass: { { 273.127, 0 }, { 237.608, 216062 } } kg +compflowStatistics: Max phase CFL number: 3.53924 +compflowStatistics: Max component CFL number: 1.60031 +Time: 2.45e+08s, dt:1e+06s, Cycle: 1139 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e+00 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Line search @ 0.408: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00623282 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.173423 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7717e+07, 1.77561e+07, 1.77928e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21807e+06, 5.29389e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.555 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.01824, 725.537 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3088.7, 703255 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.739, 213037 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2527.97, 490218 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.495, 0.00107286 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2942.21, 703255 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3088.7, 0 }, { 1128.74, 702104 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76983e+07, 1.77108e+07, 1.77357e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19943e+06, 5.23679e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.81 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.625005, 223.185 } rm^3 +compflowStatistics, caprock: Phase mass: { 274.983, 216300 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 102.542, 65073.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 172.44, 151227 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.8377, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 263.145, 216300 } kg +compflowStatistics, caprock: Dissolved component mass: { { 274.983, 0 }, { 238.299, 216057 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.6974 +compflowStatistics: Max component CFL number: 1.54788 +Time: 2.46e+08s, dt:1e+06s, Cycle: 1140 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; + Line search @ 0.421: ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.15e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00621867 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.227713 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77159e+07, 1.77551e+07, 1.77917e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21698e+06, 5.29281e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.554 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.0108, 725.544 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3085.19, 703261 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.821, 213037 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2524.37, 490225 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.779, 0.00107285 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2938.41, 703261 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3085.19, 0 }, { 1129.71, 702109 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76973e+07, 1.77098e+07, 1.77346e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19835e+06, 5.2357e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.81 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.629278, 223.181 } rm^3 +compflowStatistics, caprock: Phase mass: { 276.842, 216296 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 103.015, 65073.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 173.826, 151222 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.9741, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 264.868, 216296 } kg +compflowStatistics, caprock: Dissolved component mass: { { 276.842, 0 }, { 238.988, 216052 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.2604 +compflowStatistics: Max component CFL number: 1.57817 +Time: 2.47e+08s, dt:1e+06s, Cycle: 1141 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.79e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.28e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00625254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.213318 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77148e+07, 1.7754e+07, 1.77906e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.2159e+06, 5.29172e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.554 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 7.00332, 725.55 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3081.66, 703267 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.894, 213036 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2520.76, 490231 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.133, 0.00107283 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2934.53, 703267 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3081.66, 0 }, { 1130.7, 702114 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76962e+07, 1.77087e+07, 1.77335e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19726e+06, 5.23462e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.81 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.633557, 223.176 } rm^3 +compflowStatistics, caprock: Phase mass: { 278.702, 216291 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 103.487, 65073.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 175.216, 151218 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.9434, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 266.759, 216291 } kg +compflowStatistics, caprock: Dissolved component mass: { { 278.702, 0 }, { 239.674, 216047 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.38679 +compflowStatistics: Max component CFL number: 1.46126 +Time: 2.48e+08s, dt:1e+06s, Cycle: 1142 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.56e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.76e-03 ) ; + Line search @ 0.410: ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e+00 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00618707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.183909 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77137e+07, 1.77529e+07, 1.77895e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21481e+06, 5.29063e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.553 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.99586, 725.557 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3078.14, 703274 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.976, 213036 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2517.16, 490238 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.445, 0.00107282 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2930.69, 703274 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3078.14, 0 }, { 1131.67, 702119 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76951e+07, 1.77076e+07, 1.77324e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19617e+06, 5.23353e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.81 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.637844, 223.172 } rm^3 +compflowStatistics, caprock: Phase mass: { 280.567, 216287 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 103.958, 65073.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 176.608, 151214 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.1173, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 268.449, 216287 } kg +compflowStatistics, caprock: Dissolved component mass: { { 280.567, 0 }, { 240.357, 216042 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.87835 +compflowStatistics: Max component CFL number: 1.61544 +Time: 2.49e+08s, dt:1e+06s, Cycle: 1143 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Line search @ 0.366: ( Rflow ) = ( 2.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.183: ( Rflow ) = ( 1.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.092: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.046: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.73e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.59e-03 ) ; + Line search @ 0.381: ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.92e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00614713 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.195652 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77126e+07, 1.77518e+07, 1.77885e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21372e+06, 5.28954e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.552 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.98839, 725.564 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3074.62, 703280 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.081, 213035 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2513.54, 490244 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.908, 0.0010728 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2926.71, 703280 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3074.62, 0 }, { 1132.64, 702124 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7694e+07, 1.77065e+07, 1.77314e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19508e+06, 5.23244e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.809 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.642141, 223.167 } rm^3 +compflowStatistics, caprock: Phase mass: { 282.435, 216282 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 104.43, 65073.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 178.006, 151209 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.063, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 270.372, 216282 } kg +compflowStatistics, caprock: Dissolved component mass: { { 282.435, 0 }, { 241.035, 216037 } } kg +compflowStatistics: Max phase CFL number: 3.23344 +compflowStatistics: Max component CFL number: 1.75714 +Time: 2.5e+08s, dt:1e+06s, Cycle: 1144 +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Line search @ 0.411: ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.55e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.57e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00604757 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.181224 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77116e+07, 1.77507e+07, 1.77874e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21264e+06, 5.28846e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.551 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.981, 725.57 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3071.14, 703286 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.259, 213035 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2509.88, 490251 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.346, 0.00107279 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2922.79, 703286 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3071.14, 0 }, { 1133.58, 702130 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76929e+07, 1.77054e+07, 1.77303e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.194e+06, 5.23136e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.809 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.646446, 223.163 } rm^3 +compflowStatistics, caprock: Phase mass: { 284.307, 216278 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 104.901, 65073.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 179.406, 151205 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.2974, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 272.01, 216278 } kg +compflowStatistics, caprock: Dissolved component mass: { { 284.307, 0 }, { 241.712, 216031 } } kg +compflowStatistics: Max phase CFL number: 4.19784 +compflowStatistics: Max component CFL number: 1.62526 +Time: 2.51e+08s, dt:1e+06s, Cycle: 1145 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.09e-03 ) ; + Line search @ 0.471: ( Rflow ) = ( 2.94e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.236: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.64e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.95e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00598596 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.205986 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77105e+07, 1.77497e+07, 1.77864e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21159e+06, 5.28741e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.551 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.97361, 725.577 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3067.66, 703292 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.385, 213035 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2506.27, 490257 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.337, 0.00107278 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2919.32, 703292 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3067.66, 0 }, { 1134.51, 702135 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76919e+07, 1.77044e+07, 1.77293e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19294e+06, 5.23031e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.809 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.650762, 223.158 } rm^3 +compflowStatistics, caprock: Phase mass: { 286.184, 216274 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 105.373, 65073.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 180.811, 151200 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.3969, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 273.787, 216274 } kg +compflowStatistics, caprock: Dissolved component mass: { { 286.184, 0 }, { 242.384, 216026 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.87874 +compflowStatistics: Max component CFL number: 1.51929 +Time: 2.52e+08s, dt:1e+06s, Cycle: 1146 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.36e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.74e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.31e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00594185 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.198536 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77095e+07, 1.77487e+07, 1.77853e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.21054e+06, 5.28636e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.55 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.96623, 725.584 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3064.18, 703298 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.465, 213034 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2502.72, 490263 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.511, 0.00107276 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2915.67, 703298 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3064.18, 0 }, { 1135.43, 702140 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76908e+07, 1.77033e+07, 1.77282e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19189e+06, 5.22926e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.809 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.655086, 223.154 } rm^3 +compflowStatistics, caprock: Phase mass: { 288.064, 216269 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 105.843, 65073 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 182.221, 151196 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.3038, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 275.76, 216269 } kg +compflowStatistics, caprock: Dissolved component mass: { { 288.064, 0 }, { 243.052, 216021 } } kg +compflowStatistics: Max phase CFL number: 2.95848 +compflowStatistics: Max component CFL number: 1.26533 +Time: 2.53e+08s, dt:1e+06s, Cycle: 1147 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Line search @ 0.452: ( Rflow ) = ( 5.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.226: ( Rflow ) = ( 2.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.113: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.11e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00596673 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.21275 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77084e+07, 1.77476e+07, 1.77843e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20949e+06, 5.28532e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.549 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.95884, 725.59 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3060.7, 703304 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.527, 213034 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2499.18, 490270 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.752, 0.00107275 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2911.95, 703304 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3060.7, 0 }, { 1136.36, 702145 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76898e+07, 1.77023e+07, 1.77272e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.19085e+06, 5.22821e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.808 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.659412, 223.149 } rm^3 +compflowStatistics, caprock: Phase mass: { 289.945, 216265 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 106.308, 65073 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 183.636, 151192 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.3828, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 277.562, 216265 } kg +compflowStatistics, caprock: Dissolved component mass: { { 289.945, 0 }, { 243.72, 216016 } } kg +compflowStatistics: Max phase CFL number: 2.88234 +compflowStatistics: Max component CFL number: 1.26859 +Time: 2.54e+08s, dt:1e+06s, Cycle: 1148 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.36e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.56e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Line search @ 0.365: ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.39e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.39e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.96e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00589484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.207986 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77074e+07, 1.77466e+07, 1.77832e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20844e+06, 5.28427e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.548 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.95148, 725.597 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3057.24, 703310 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.562, 213034 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2495.68, 490276 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.667, 0.00107274 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2908.57, 703310 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3057.24, 0 }, { 1137.27, 702150 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76888e+07, 1.77012e+07, 1.77261e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1898e+06, 5.22717e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.808 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.66374, 223.144 } rm^3 +compflowStatistics, caprock: Phase mass: { 291.826, 216260 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 106.768, 65072.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 185.058, 151187 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.2592, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 279.567, 216260 } kg +compflowStatistics, caprock: Dissolved component mass: { { 291.826, 0 }, { 244.392, 216011 } } kg +compflowStatistics: Max phase CFL number: 2.98302 +compflowStatistics: Max component CFL number: 1.2753 +Time: 2.55e+08s, dt:1e+06s, Cycle: 1149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.27e-03 ) ; + Line search @ 0.443: ( Rflow ) = ( 1.88e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.222: ( Rflow ) = ( 1.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.95e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.72e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e+00 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e+00 ) ; + Last LinSolve(iter,res) = ( 4, 6.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.50e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 9.95e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.95e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.05e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.05e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00582023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.186146 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77064e+07, 1.77456e+07, 1.77822e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20741e+06, 5.28323e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.548 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.94417, 725.603 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3053.81, 703316 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.617, 213033 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2492.19, 490283 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.775, 0.00107273 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2905.03, 703316 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3053.81, 0 }, { 1138.15, 702155 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76877e+07, 1.77002e+07, 1.77251e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18876e+06, 5.22613e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.808 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.668076, 223.14 } rm^3 +compflowStatistics, caprock: Phase mass: { 293.711, 216256 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 107.226, 65072.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 186.485, 151183 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.3588, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 281.353, 216256 } kg +compflowStatistics, caprock: Dissolved component mass: { { 293.711, 0 }, { 245.061, 216006 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.13292 +compflowStatistics: Max component CFL number: 1.29788 +Time: 2.56e+08s, dt:1e+06s, Cycle: 1150 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.412: ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.206: ( Rflow ) = ( 9.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.19e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.98e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00577387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.18074 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77054e+07, 1.77445e+07, 1.77812e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20639e+06, 5.28222e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.547 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.93686, 725.61 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3050.37, 703322 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.625, 213033 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2488.75, 490289 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.854, 0.00107271 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2901.52, 703322 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3050.37, 0 }, { 1139.03, 702160 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76867e+07, 1.76992e+07, 1.77241e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18774e+06, 5.22512e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.808 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.672417, 223.135 } rm^3 +compflowStatistics, caprock: Phase mass: { 295.599, 216251 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 107.676, 65072.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 187.923, 151179 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 12.0849, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 283.514, 216251 } kg +compflowStatistics, caprock: Dissolved component mass: { { 295.599, 0 }, { 245.729, 216001 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.8698 +compflowStatistics: Max component CFL number: 1.32537 +Time: 2.57e+08s, dt:1e+06s, Cycle: 1151 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.76e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Line search @ 0.411: ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.206: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.103: ( Rflow ) = ( 9.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.68e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Line search @ 0.464: ( Rflow ) = ( 2.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.232: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.116: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.058: ( Rflow ) = ( 9.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.70e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.57e-03 ) ; + Line search @ 0.496: ( Rflow ) = ( 2.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.248: ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.124: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.15e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.77e-03 ) ; + Last LinSolve(iter,res) = ( 7, 3.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 6.97e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.97e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0057546 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.190662 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77044e+07, 1.77435e+07, 1.77802e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20538e+06, 5.2812e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.546 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.92955, 725.616 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3046.93, 703328 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.638, 213033 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2485.3, 490295 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.925, 0.0010727 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2898.01, 703328 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3046.93, 0 }, { 1139.92, 702165 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76857e+07, 1.76982e+07, 1.77231e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18673e+06, 5.2241e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.808 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.676768, 223.131 } rm^3 +compflowStatistics, caprock: Phase mass: { 297.49, 216247 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 108.12, 65072.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 189.37, 151174 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.84, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 285.65, 216247 } kg +compflowStatistics, caprock: Dissolved component mass: { { 297.49, 0 }, { 246.39, 215996 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.03564 +compflowStatistics: Max component CFL number: 1.33801 +Time: 2.58e+08s, dt:1e+06s, Cycle: 1152 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.442: ( Rflow ) = ( 9.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.75e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00571208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.194916 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77034e+07, 1.77425e+07, 1.77792e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20437e+06, 5.28019e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.545 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.92225, 725.623 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3043.51, 703334 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.663, 213032 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2481.85, 490302 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.911, 0.00107269 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2894.6, 703334 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3043.51, 0 }, { 1140.79, 702171 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76847e+07, 1.76972e+07, 1.77221e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18571e+06, 5.22309e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.807 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.681123, 223.126 } rm^3 +compflowStatistics, caprock: Phase mass: { 299.383, 216242 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 108.556, 65072.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 190.827, 151170 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.698, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 287.685, 216242 } kg +compflowStatistics, caprock: Dissolved component mass: { { 299.383, 0 }, { 247.051, 215990 } } kg +compflowStatistics: Max phase CFL number: 4.84687 +compflowStatistics: Max component CFL number: 1.50021 +Time: 2.59e+08s, dt:1e+06s, Cycle: 1153 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.14e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.14e-07 ) ; + Last LinSolve(iter,res) = ( 9, 9.88e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00564642 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.18914 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77024e+07, 1.77415e+07, 1.77782e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20336e+06, 5.27919e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.545 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.915, 725.63 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3040.11, 703340 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.703, 213032 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2478.41, 490308 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.816, 0.00107268 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2891.29, 703340 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3040.11, 0 }, { 1141.63, 702176 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76837e+07, 1.76962e+07, 1.77211e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18471e+06, 5.22208e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.807 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.685488, 223.122 } rm^3 +compflowStatistics, caprock: Phase mass: { 301.281, 216238 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 108.989, 65072.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 192.292, 151165 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.4638, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 289.817, 216238 } kg +compflowStatistics, caprock: Dissolved component mass: { { 301.281, 0 }, { 247.708, 215985 } } kg +compflowStatistics: Max phase CFL number: 4.96256 +compflowStatistics: Max component CFL number: 1.51786 +Time: 2.6e+08s, dt:1e+06s, Cycle: 1154 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.61e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Line search @ 0.405: ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.45e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.45e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 4.20e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0056005 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.210693 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.77014e+07, 1.77406e+07, 1.77772e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20238e+06, 5.2782e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.544 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.90775, 725.636 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3036.71, 703346 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.719, 213032 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2474.99, 490314 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.748, 0.00107267 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2887.96, 703346 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3036.71, 0 }, { 1142.48, 702181 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76827e+07, 1.76952e+07, 1.77201e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18372e+06, 5.2211e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.807 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.689864, 223.117 } rm^3 +compflowStatistics, caprock: Phase mass: { 303.182, 216234 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 109.418, 65072.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 193.764, 151161 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.2851, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 291.897, 216234 } kg +compflowStatistics, caprock: Dissolved component mass: { { 303.182, 0 }, { 248.358, 215980 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.26473 +compflowStatistics: Max component CFL number: 1.4405 +Time: 2.61e+08s, dt:1e+06s, Cycle: 1155 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.48e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.389: ( Rflow ) = ( 8.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.06e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00555483 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.239483 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.77004e+07, 1.77396e+07, 1.77762e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20139e+06, 5.27722e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.543 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.90052, 725.643 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3033.32, 703352 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.704, 213031 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2471.62, 490321 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.575, 0.00107265 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2884.75, 703352 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3033.32, 0 }, { 1143.32, 702186 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76818e+07, 1.76942e+07, 1.77191e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18273e+06, 5.22011e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.807 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.694246, 223.112 } rm^3 +compflowStatistics, caprock: Phase mass: { 305.087, 216229 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 109.843, 65072.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 195.245, 151157 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.1931, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 293.894, 216229 } kg +compflowStatistics, caprock: Dissolved component mass: { { 305.087, 0 }, { 249.004, 215975 } } kg +compflowStatistics: Max phase CFL number: 3.20584 +compflowStatistics: Max component CFL number: 1.16872 +Time: 2.62e+08s, dt:1e+06s, Cycle: 1156 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.61e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.64e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00556347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.186379 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76994e+07, 1.77386e+07, 1.77753e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.20042e+06, 5.27624e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.542 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.89328, 725.649 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3029.93, 703358 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.703, 213031 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2468.23, 490327 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.495, 0.00107264 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2881.43, 703358 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3029.93, 0 }, { 1144.16, 702191 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76808e+07, 1.76933e+07, 1.77182e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18176e+06, 5.21914e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.806 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.698633, 223.108 } rm^3 +compflowStatistics, caprock: Phase mass: { 306.994, 216225 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 110.261, 65072.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 196.733, 151152 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9744, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 296.02, 216225 } kg +compflowStatistics, caprock: Dissolved component mass: { { 306.994, 0 }, { 249.648, 215970 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.18896 +compflowStatistics: Max component CFL number: 1.157 +Time: 2.63e+08s, dt:1e+06s, Cycle: 1157 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.439: ( Rflow ) = ( 8.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.220: ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.110: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.01e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.58e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.00e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.87e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 4.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-04 ) ; + Last LinSolve(iter,res) = ( 6, 2.73e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00546149 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.150745 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76985e+07, 1.77377e+07, 1.77743e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19944e+06, 5.27527e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.542 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.8861, 725.656 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3026.57, 703364 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.748, 213031 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2464.82, 490333 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.437, 0.00107263 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2878.13, 703364 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3026.57, 0 }, { 1144.97, 702196 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76798e+07, 1.76923e+07, 1.77172e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.18078e+06, 5.21816e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.806 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.703029, 223.103 } rm^3 +compflowStatistics, caprock: Phase mass: { 308.904, 216220 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 110.675, 65072.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 198.229, 151148 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.8897, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 298.015, 216220 } kg +compflowStatistics, caprock: Dissolved component mass: { { 308.904, 0 }, { 250.29, 215965 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.9684 +compflowStatistics: Max component CFL number: 1.17639 +Time: 2.64e+08s, dt:1e+06s, Cycle: 1158 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e+00 ) ; + Last LinSolve(iter,res) = ( 4, 4.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.44e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.76e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.76e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00538801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.154545 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76975e+07, 1.77367e+07, 1.77734e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19849e+06, 5.27432e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.541 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.87895, 725.662 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3023.22, 703370 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.807, 213030 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2461.42, 490340 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.302, 0.00107262 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2874.92, 703370 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3023.22, 0 }, { 1145.76, 702201 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76789e+07, 1.76914e+07, 1.77163e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17983e+06, 5.21721e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.806 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.707429, 223.099 } rm^3 +compflowStatistics, caprock: Phase mass: { 310.817, 216216 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 111.087, 65072.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 199.73, 151143 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.7686, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 300.048, 216216 } kg +compflowStatistics, caprock: Dissolved component mass: { { 310.817, 0 }, { 250.93, 215960 } } kg +compflowStatistics: Max phase CFL number: 5.3137 +compflowStatistics: Max component CFL number: 1.13789 +Time: 2.65e+08s, dt:1e+06s, Cycle: 1159 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +well_1Control: well is shut + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.11e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.68e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.68e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00537864 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.149068 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76966e+07, 1.77358e+07, 1.77724e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19755e+06, 5.27338e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.54 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.87179, 725.669 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3019.87, 703376 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.827, 213030 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2458.04, 490346 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.045, 0.00107262 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2871.83, 703376 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3019.87, 0 }, { 1146.56, 702207 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76779e+07, 1.76904e+07, 1.77153e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17888e+06, 5.21627e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.806 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.711826, 223.094 } rm^3 +compflowStatistics, caprock: Phase mass: { 312.728, 216211 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 111.49, 65072.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 201.238, 151139 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.688, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 302.04, 216211 } kg +compflowStatistics, caprock: Dissolved component mass: { { 312.728, 0 }, { 251.575, 215954 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.82084 +compflowStatistics: Max component CFL number: 1.24419 +Time: 2.66e+08s, dt:1e+06s, Cycle: 1160 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.95e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.476: ( Rflow ) = ( 2.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.238: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.119: ( Rflow ) = ( 8.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.89e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.56e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.18e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.18e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00546197 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.180296 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76956e+07, 1.77348e+07, 1.77715e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1966e+06, 5.27243e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.54 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.86459, 725.675 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3016.5, 703382 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.809, 213030 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2454.69, 490352 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.806, 0.00107261 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2868.7, 703382 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3016.5, 0 }, { 1147.37, 702212 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7677e+07, 1.76895e+07, 1.77144e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17794e+06, 5.21533e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.806 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.716223, 223.089 } rm^3 +compflowStatistics, caprock: Phase mass: { 314.638, 216207 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 111.886, 65072.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 202.752, 151134 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.4244, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 304.213, 216207 } kg +compflowStatistics, caprock: Dissolved component mass: { { 314.638, 0 }, { 252.22, 215949 } } kg +compflowStatistics: Max phase CFL number: 3.9217 +compflowStatistics: Max component CFL number: 1.32278 +Time: 2.67e+08s, dt:1e+06s, Cycle: 1161 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.34e-03 ) ; + Line search @ 0.424: ( Rflow ) = ( 8.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.68e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.71e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.33e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0053905 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.194471 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76947e+07, 1.77339e+07, 1.77705e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19565e+06, 5.27147e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.539 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.85743, 725.682 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3013.15, 703388 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.789, 213029 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2451.36, 490358 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.641, 0.0010726 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2865.51, 703388 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3013.15, 0 }, { 1148.17, 702217 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7676e+07, 1.76885e+07, 1.77134e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17698e+06, 5.21437e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.805 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.720625, 223.085 } rm^3 +compflowStatistics, caprock: Phase mass: { 316.551, 216202 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 112.272, 65072.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 204.279, 151130 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.01, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 306.541, 216202 } kg +compflowStatistics, caprock: Dissolved component mass: { { 316.551, 0 }, { 252.862, 215944 } } kg +compflowStatistics: Max phase CFL number: 3.50893 +compflowStatistics: Max component CFL number: 1.15713 +Time: 2.68e+08s, dt:1e+06s, Cycle: 1162 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.38e-03 ) ; + Line search @ 0.467: ( Rflow ) = ( 1.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.233: ( Rflow ) = ( 9.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.64e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.54e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00539425 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.182648 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76938e+07, 1.77329e+07, 1.77696e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1947e+06, 5.27053e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.538 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.85025, 725.688 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3009.79, 703394 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.749, 213029 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2448.04, 490365 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.379, 0.00107259 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2862.41, 703394 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3009.79, 0 }, { 1148.98, 702222 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76751e+07, 1.76876e+07, 1.77125e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17604e+06, 5.21342e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.805 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.725037, 223.08 } rm^3 +compflowStatistics, caprock: Phase mass: { 318.467, 216198 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 112.655, 65072.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 205.812, 151126 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.89018, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 308.577, 216198 } kg +compflowStatistics, caprock: Dissolved component mass: { { 318.467, 0 }, { 253.497, 215939 } } kg +compflowStatistics: Max phase CFL number: 4.80104 +compflowStatistics: Max component CFL number: 1.46093 +Time: 2.69e+08s, dt:1e+06s, Cycle: 1163 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.89e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.77e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.77e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.05e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0053181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.218175 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76928e+07, 1.7732e+07, 1.77686e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19375e+06, 5.26958e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.538 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.84311, 725.695 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3006.46, 703400 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.719, 213029 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2444.74, 490371 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.195, 0.00107258 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2859.26, 703400 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3006.46, 0 }, { 1149.76, 702227 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76742e+07, 1.76866e+07, 1.77115e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17509e+06, 5.21248e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.805 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.729452, 223.076 } rm^3 +compflowStatistics, caprock: Phase mass: { 320.385, 216193 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 113.032, 65072.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 207.352, 151121 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.71261, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 310.672, 216193 } kg +compflowStatistics, caprock: Dissolved component mass: { { 320.385, 0 }, { 254.131, 215934 } } kg +compflowStatistics: Max phase CFL number: 3.71938 +compflowStatistics: Max component CFL number: 1.75199 +Time: 2.7e+08s, dt:1e+06s, Cycle: 1164 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; + Line search @ 0.367: ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.98e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.16e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00526809 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.160052 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76919e+07, 1.77311e+07, 1.77677e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19282e+06, 5.26865e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.537 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.836, 725.701 } rm^3 +compflowStatistics, reservoir: Phase mass: { 3003.13, 703406 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.696, 213028 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2441.44, 490377 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.989, 0.00107257 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2856.14, 703406 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 3003.13, 0 }, { 1150.53, 702232 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76732e+07, 1.76857e+07, 1.77106e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17416e+06, 5.21155e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.805 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.733871, 223.071 } rm^3 +compflowStatistics, caprock: Phase mass: { 322.305, 216189 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 113.408, 65072 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 208.896, 151117 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.67397, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 312.631, 216189 } kg +compflowStatistics, caprock: Dissolved component mass: { { 322.305, 0 }, { 254.764, 215929 } } kg +compflowStatistics: Max phase CFL number: 1.77396 +compflowStatistics: Max component CFL number: 1.67153 +Time: 2.71e+08s, dt:1e+06s, Cycle: 1165 +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Line search @ 0.475: ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.238: ( Rflow ) = ( 9.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 8.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.93e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.93e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00521237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.181686 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7691e+07, 1.77302e+07, 1.77668e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1919e+06, 5.26773e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.536 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.82891, 725.707 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2999.83, 703412 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.686, 213028 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2438.14, 490383 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.804, 0.00107256 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2853.02, 703412 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2999.83, 0 }, { 1151.28, 702237 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76723e+07, 1.76848e+07, 1.77097e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17323e+06, 5.21062e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.805 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.738291, 223.066 } rm^3 +compflowStatistics, caprock: Phase mass: { 324.225, 216184 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 113.779, 65072 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 210.445, 151112 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.56366, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 314.661, 216184 } kg +compflowStatistics, caprock: Dissolved component mass: { { 324.225, 0 }, { 255.399, 215924 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.86217 +compflowStatistics: Max component CFL number: 1.64656 +Time: 2.72e+08s, dt:1e+06s, Cycle: 1166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.396: ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00514922 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.163743 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.76901e+07, 1.77293e+07, 1.77659e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19099e+06, 5.26681e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.536 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.82186, 725.714 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2996.54, 703417 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.67, 213028 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2434.87, 490390 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.647, 0.00107255 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2849.89, 703417 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2996.54, 0 }, { 1152.01, 702242 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76714e+07, 1.76839e+07, 1.77088e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17232e+06, 5.20971e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.804 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.742713, 223.062 } rm^3 +compflowStatistics, caprock: Phase mass: { 326.146, 216180 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 114.144, 65071.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 212.002, 151108 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.42466, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 316.721, 216180 } kg +compflowStatistics, caprock: Dissolved component mass: { { 326.146, 0 }, { 256.036, 215919 } } kg +compflowStatistics: Max phase CFL number: 3.97665 +compflowStatistics: Max component CFL number: 1.43208 +Time: 2.73e+08s, dt:1e+06s, Cycle: 1167 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.57e-03 ) ; + Line search @ 0.356: ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.14e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00519943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.186122 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76892e+07, 1.77283e+07, 1.7765e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.19009e+06, 5.26592e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.535 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.81478, 725.72 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2993.23, 703423 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.623, 213028 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2431.61, 490396 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.394, 0.00107254 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2846.84, 703423 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2993.23, 0 }, { 1152.76, 702248 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76705e+07, 1.7683e+07, 1.77079e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17142e+06, 5.20881e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.804 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.747129, 223.057 } rm^3 +compflowStatistics, caprock: Phase mass: { 328.064, 216175 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 114.5, 65071.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 213.563, 151103 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.20995, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 318.854, 216175 } kg +compflowStatistics, caprock: Dissolved component mass: { { 328.064, 0 }, { 256.677, 215913 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.02165 +compflowStatistics: Max component CFL number: 1.34808 +Time: 2.74e+08s, dt:1e+06s, Cycle: 1168 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.435: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.62e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.62e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00523867 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.160062 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76883e+07, 1.77274e+07, 1.77641e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18918e+06, 5.265e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.534 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.80768, 725.727 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2989.92, 703429 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.554, 213027 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2428.36, 490402 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.28, 0.00107253 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2843.64, 703429 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2989.92, 0 }, { 1153.52, 702253 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76696e+07, 1.76821e+07, 1.7707e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.17051e+06, 5.2079e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.804 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.751539, 223.052 } rm^3 +compflowStatistics, caprock: Phase mass: { 329.978, 216171 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 114.849, 65071.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 215.129, 151099 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.08708, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 320.891, 216171 } kg +compflowStatistics, caprock: Dissolved component mass: { { 329.978, 0 }, { 257.323, 215908 } } kg +compflowStatistics: Max phase CFL number: 5.08294 +compflowStatistics: Max component CFL number: 1.30631 +Time: 2.75e+08s, dt:1e+06s, Cycle: 1169 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.43e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.55e-03 ) ; + Line search @ 0.412: ( Rflow ) = ( 2.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.206: ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.103: ( Rflow ) = ( 9.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 6.42e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.42e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00526575 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.20492 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76873e+07, 1.77265e+07, 1.77632e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18825e+06, 5.26408e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.534 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.80057, 725.733 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2986.59, 703435 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.488, 213027 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2425.11, 490408 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.061, 0.00107253 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2840.53, 703435 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2986.59, 0 }, { 1154.27, 702258 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76687e+07, 1.76811e+07, 1.77061e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16959e+06, 5.20698e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.804 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.755944, 223.048 } rm^3 +compflowStatistics, caprock: Phase mass: { 331.89, 216166 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 115.194, 65071.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 216.696, 151094 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.06452, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 322.826, 216166 } kg +compflowStatistics, caprock: Dissolved component mass: { { 331.89, 0 }, { 257.973, 215903 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.49909 +compflowStatistics: Max component CFL number: 1.23862 +Time: 2.76e+08s, dt:1e+06s, Cycle: 1170 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; + Line search @ 0.397: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.198: ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.53e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.53e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.12e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00519536 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.187464 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76864e+07, 1.77256e+07, 1.77622e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18733e+06, 5.26315e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.533 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.79349, 725.739 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2983.29, 703441 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.452, 213027 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2421.84, 490414 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.995, 0.00107252 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2837.3, 703441 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2983.29, 0 }, { 1155.01, 702263 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76677e+07, 1.76802e+07, 1.77051e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16866e+06, 5.20605e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.804 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.760354, 223.043 } rm^3 +compflowStatistics, caprock: Phase mass: { 333.805, 216162 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 115.539, 65071.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 218.266, 151090 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.12501, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 324.68, 216162 } kg +compflowStatistics, caprock: Dissolved component mass: { { 333.805, 0 }, { 258.62, 215898 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 5.31406 +compflowStatistics: Max component CFL number: 1.79069 +Time: 2.77e+08s, dt:1e+06s, Cycle: 1171 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.97e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Line search @ 0.381: ( Rflow ) = ( 8.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.58e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00516541 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.239681 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76855e+07, 1.77247e+07, 1.77613e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18641e+06, 5.26224e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.532 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.78642, 725.746 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2979.99, 703447 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.416, 213026 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2418.58, 490421 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.793, 0.00107251 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2834.2, 703447 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2979.99, 0 }, { 1155.75, 702268 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76668e+07, 1.76793e+07, 1.77042e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16775e+06, 5.20514e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.803 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.764773, 223.039 } rm^3 +compflowStatistics, caprock: Phase mass: { 335.723, 216157 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 115.884, 65071.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 219.839, 151086 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.07142, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 326.652, 216157 } kg +compflowStatistics, caprock: Dissolved component mass: { { 335.723, 0 }, { 259.261, 215893 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.09952 +compflowStatistics: Max component CFL number: 2.15802 +Time: 2.78e+08s, dt:1e+06s, Cycle: 1172 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.63e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.63e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.84e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.96e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.49e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00523597 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.196448 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76846e+07, 1.77238e+07, 1.77604e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18551e+06, 5.26134e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.532 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.77933, 725.752 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2976.68, 703453 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.37, 213026 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2415.31, 490427 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.706, 0.0010725 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2830.98, 703453 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2976.68, 0 }, { 1156.51, 702273 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76659e+07, 1.76784e+07, 1.77033e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16684e+06, 5.20423e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.803 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.769191, 223.034 } rm^3 +compflowStatistics, caprock: Phase mass: { 337.64, 216153 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 116.225, 65071.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 221.416, 151081 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.89316, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 328.747, 216153 } kg +compflowStatistics, caprock: Dissolved component mass: { { 337.64, 0 }, { 259.902, 215888 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.94786 +compflowStatistics: Max component CFL number: 1.74854 +Time: 2.79e+08s, dt:1e+06s, Cycle: 1173 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.53e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.45e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.45e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.97e-03 ) ; + Last LinSolve(iter,res) = ( 8, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00522753 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.143359 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76837e+07, 1.77228e+07, 1.77595e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18459e+06, 5.26042e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.531 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.77223, 725.759 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2973.37, 703459 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.341, 213026 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2412.03, 490433 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.705, 0.0010725 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2827.67, 703459 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2973.37, 0 }, { 1157.26, 702278 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7665e+07, 1.76775e+07, 1.77024e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16592e+06, 5.20332e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.803 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.773621, 223.029 } rm^3 +compflowStatistics, caprock: Phase mass: { 339.563, 216148 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 116.563, 65071.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 223, 151077 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.6608, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 330.902, 216148 } kg +compflowStatistics, caprock: Dissolved component mass: { { 339.563, 0 }, { 260.532, 215883 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.4561 +compflowStatistics: Max component CFL number: 2.31326 +Time: 2.8e+08s, dt:1e+06s, Cycle: 1174 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.54e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.54e+00 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.77e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.51e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.51e-06 ) ; + Last LinSolve(iter,res) = ( 6, 3.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00510958 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.162416 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76828e+07, 1.7722e+07, 1.77586e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18368e+06, 5.2595e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.53 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.76519, 725.765 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2970.1, 703465 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.358, 213025 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2408.74, 490439 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.494, 0.00107249 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2824.6, 703465 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2970.1, 0 }, { 1157.99, 702284 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76641e+07, 1.76766e+07, 1.77015e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16501e+06, 5.2024e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.803 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.778057, 223.025 } rm^3 +compflowStatistics, caprock: Phase mass: { 341.488, 216144 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 116.9, 65071.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 224.588, 151072 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.56704, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 332.921, 216144 } kg +compflowStatistics, caprock: Dissolved component mass: { { 341.488, 0 }, { 261.159, 215877 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.04455 +compflowStatistics: Max component CFL number: 2.64185 +Time: 2.81e+08s, dt:1e+06s, Cycle: 1175 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.96e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.00e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00508507 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.173567 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.76819e+07, 1.77211e+07, 1.77577e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18279e+06, 5.25862e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.53 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.75815, 725.772 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2966.81, 703470 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.377, 213025 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2405.44, 490445 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.487, 0.00107248 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2821.33, 703470 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2966.81, 0 }, { 1158.72, 702289 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76632e+07, 1.76757e+07, 1.77006e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16412e+06, 5.20151e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.803 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.782493, 223.02 } rm^3 +compflowStatistics, caprock: Phase mass: { 343.413, 216139 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 117.231, 65071.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 226.182, 151068 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.43323, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 334.98, 216139 } kg +compflowStatistics, caprock: Dissolved component mass: { { 343.413, 0 }, { 261.788, 215872 } } kg +compflowStatistics: Max phase CFL number: 4.35099 +compflowStatistics: Max component CFL number: 2.78985 +Time: 2.82e+08s, dt:1e+06s, Cycle: 1176 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.77e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.80e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.80e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00510866 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.157368 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7681e+07, 1.77202e+07, 1.77568e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18189e+06, 5.25772e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.529 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.75109, 725.778 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2963.53, 703476 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.376, 213025 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2402.15, 490452 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.267, 0.00107247 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2818.26, 703476 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2963.53, 0 }, { 1159.45, 702294 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76623e+07, 1.76748e+07, 1.76997e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16322e+06, 5.20062e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.802 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.786926, 223.015 } rm^3 +compflowStatistics, caprock: Phase mass: { 345.337, 216135 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 117.558, 65071.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 227.779, 151063 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.25609, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 337.08, 216135 } kg +compflowStatistics, caprock: Dissolved component mass: { { 345.337, 0 }, { 262.417, 215867 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.07047 +compflowStatistics: Max component CFL number: 2.51229 +Time: 2.83e+08s, dt:1e+06s, Cycle: 1177 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.47e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.90e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.48e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.71e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00506288 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.144397 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76801e+07, 1.77193e+07, 1.77559e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.18099e+06, 5.25682e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.528 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.74406, 725.784 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2960.25, 703482 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.37, 213024 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2398.88, 490458 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.063, 0.00107246 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2815.19, 703482 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2960.25, 0 }, { 1160.17, 702299 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76614e+07, 1.76739e+07, 1.76988e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16232e+06, 5.19972e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.802 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.79136, 223.011 } rm^3 +compflowStatistics, caprock: Phase mass: { 347.26, 216130 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 117.88, 65071.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 229.38, 151059 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.18768, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 339.073, 216130 } kg +compflowStatistics, caprock: Dissolved component mass: { { 347.26, 0 }, { 263.046, 215862 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.68248 +compflowStatistics: Max component CFL number: 2.1425 +Time: 2.84e+08s, dt:1e+06s, Cycle: 1178 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.34e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.99e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 2.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.48e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00513957 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.144428 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76792e+07, 1.77184e+07, 1.7755e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1801e+06, 5.25593e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.528 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.73699, 725.791 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2956.96, 703488 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.344, 213024 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2395.62, 490464 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.925, 0.00107245 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2812.03, 703488 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2956.96, 0 }, { 1160.91, 702304 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76605e+07, 1.7673e+07, 1.76979e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16143e+06, 5.19883e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.802 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.795792, 223.006 } rm^3 +compflowStatistics, caprock: Phase mass: { 349.182, 216126 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 118.2, 65071.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 230.982, 151054 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.13368, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 341.049, 216126 } kg +compflowStatistics, caprock: Dissolved component mass: { { 349.182, 0 }, { 263.676, 215857 } } kg +compflowStatistics: Max phase CFL number: 3.53343 +compflowStatistics: Max component CFL number: 1.74245 +Time: 2.85e+08s, dt:1e+06s, Cycle: 1179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.419: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.24e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.03e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00507 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.201113 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76783e+07, 1.77175e+07, 1.77541e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1792e+06, 5.25503e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.527 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.72996, 725.797 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2953.69, 703494 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.321, 213024 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2392.36, 490470 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.739, 0.00107244 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2808.95, 703494 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2953.69, 0 }, { 1161.63, 702309 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76596e+07, 1.76721e+07, 1.7697e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.16053e+06, 5.19793e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.802 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.800224, 223.002 } rm^3 +compflowStatistics, caprock: Phase mass: { 351.105, 216121 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 118.517, 65071.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 232.587, 151050 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.10969, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 342.995, 216121 } kg +compflowStatistics, caprock: Dissolved component mass: { { 351.105, 0 }, { 264.307, 215852 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.6124 +compflowStatistics: Max component CFL number: 1.41945 +Time: 2.86e+08s, dt:1e+06s, Cycle: 1180 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.31e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.396: ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.19e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00502262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.204935 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76774e+07, 1.77166e+07, 1.77533e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17831e+06, 5.25414e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.526 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.72296, 725.803 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2950.43, 703500 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.316, 213023 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2389.11, 490476 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.643, 0.00107243 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2805.79, 703500 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2950.43, 0 }, { 1162.34, 702314 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76588e+07, 1.76712e+07, 1.76962e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15964e+06, 5.19704e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.802 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.804656, 222.997 } rm^3 +compflowStatistics, caprock: Phase mass: { 353.027, 216117 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 118.83, 65071.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 234.197, 151046 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.9643, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 345.063, 216117 } kg +compflowStatistics, caprock: Dissolved component mass: { { 353.027, 0 }, { 264.938, 215847 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.50597 +compflowStatistics: Max component CFL number: 1.33962 +Time: 2.87e+08s, dt:1e+06s, Cycle: 1181 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.50e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.36e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.20e-03 ) ; + Line search @ 0.466: ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.86e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.37e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.14e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 3.50e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00504495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.151906 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76765e+07, 1.77157e+07, 1.77524e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17743e+06, 5.25326e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.526 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.71595, 725.81 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2947.17, 703506 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.319, 213023 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2385.85, 490482 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.586, 0.00107242 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2802.58, 703506 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2947.17, 0 }, { 1163.04, 702320 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76579e+07, 1.76703e+07, 1.76953e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15876e+06, 5.19616e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.801 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.809082, 222.992 } rm^3 +compflowStatistics, caprock: Phase mass: { 354.947, 216112 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 119.138, 65071.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 235.808, 151041 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.88193, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 347.065, 216112 } kg +compflowStatistics, caprock: Dissolved component mass: { { 354.947, 0 }, { 265.574, 215841 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.68858 +compflowStatistics: Max component CFL number: 1.68211 +Time: 2.88e+08s, dt:1e+06s, Cycle: 1182 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Line search @ 0.446: ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.71e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00501254 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.194289 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76757e+07, 1.77148e+07, 1.77515e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17655e+06, 5.25238e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.525 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.70896, 725.816 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2943.91, 703512 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.323, 213023 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2382.59, 490489 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.479, 0.00107241 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2799.43, 703512 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2943.91, 0 }, { 1163.75, 702325 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7657e+07, 1.76695e+07, 1.76944e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15788e+06, 5.19527e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.801 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.813514, 222.988 } rm^3 +compflowStatistics, caprock: Phase mass: { 356.869, 216108 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 119.449, 65071.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 237.42, 151037 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.96513, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 348.903, 216108 } kg +compflowStatistics, caprock: Dissolved component mass: { { 356.869, 0 }, { 266.205, 215836 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.54107 +compflowStatistics: Max component CFL number: 1.92134 +Time: 2.89e+08s, dt:1e+06s, Cycle: 1183 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.79e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Line search @ 0.449: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.00e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00496119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.156065 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76748e+07, 1.7714e+07, 1.77506e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17567e+06, 5.2515e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.525 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.70197, 725.823 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2940.66, 703517 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.318, 213023 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2379.34, 490495 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.292, 0.0010724 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2796.37, 703517 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2940.66, 0 }, { 1164.45, 702330 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76561e+07, 1.76686e+07, 1.76935e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.157e+06, 5.19439e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.801 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.817963, 222.983 } rm^3 +compflowStatistics, caprock: Phase mass: { 358.798, 216103 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 119.765, 65071.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 239.033, 151032 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.91224, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 350.886, 216103 } kg +compflowStatistics, caprock: Dissolved component mass: { { 358.798, 0 }, { 266.819, 215831 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.42295 +compflowStatistics: Max component CFL number: 1.92267 +Time: 2.9e+08s, dt:1e+06s, Cycle: 1184 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.36e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.46e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.46e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00490508 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.158411 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76739e+07, 1.77131e+07, 1.77498e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1748e+06, 5.25063e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.524 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.69501, 725.829 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2937.43, 703523 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.316, 213022 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2376.12, 490501 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.139, 0.00107239 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2793.29, 703523 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2937.43, 0 }, { 1165.14, 702335 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76553e+07, 1.76677e+07, 1.76927e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15612e+06, 5.19353e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.801 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.822419, 222.978 } rm^3 +compflowStatistics, caprock: Phase mass: { 360.73, 216099 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 120.082, 65071.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 240.648, 151028 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.90862, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 352.822, 216099 } kg +compflowStatistics, caprock: Dissolved component mass: { { 360.73, 0 }, { 267.429, 215826 } } kg +compflowStatistics: Max phase CFL number: 2.86052 +compflowStatistics: Max component CFL number: 1.53073 +Time: 2.91e+08s, dt:1e+06s, Cycle: 1185 +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Line search @ 0.316: ( Rflow ) = ( 7.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.74e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.16e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.92e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00484145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.177352 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76731e+07, 1.77123e+07, 1.77489e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17394e+06, 5.24977e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.523 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.68809, 725.835 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2934.22, 703529 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.332, 213022 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2372.89, 490507 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.066, 0.00107239 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2790.15, 703529 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2934.22, 0 }, { 1165.81, 702340 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76544e+07, 1.76669e+07, 1.76918e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15527e+06, 5.19267e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.801 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.826876, 222.974 } rm^3 +compflowStatistics, caprock: Phase mass: { 362.663, 216094 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 120.397, 65071 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 242.266, 151023 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.94162, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 354.722, 216094 } kg +compflowStatistics, caprock: Dissolved component mass: { { 362.663, 0 }, { 268.038, 215821 } } kg +compflowStatistics: Max phase CFL number: 2.81599 +compflowStatistics: Max component CFL number: 1.37996 +Time: 2.92e+08s, dt:1e+06s, Cycle: 1186 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.453: ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.41e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.95e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.95e-06 ) ; + Last LinSolve(iter,res) = ( 5, 9.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0047754 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.159809 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76723e+07, 1.77114e+07, 1.77481e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1731e+06, 5.24893e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.523 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.6812, 725.842 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2931.02, 703535 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.346, 213022 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2369.67, 490513 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.937, 0.00107238 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2787.08, 703535 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2931.02, 0 }, { 1166.47, 702345 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76536e+07, 1.7666e+07, 1.7691e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15442e+06, 5.19183e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.8 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.831345, 222.969 } rm^3 +compflowStatistics, caprock: Phase mass: { 364.602, 216090 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 120.714, 65071 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 243.888, 151019 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.85664, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 356.745, 216090 } kg +compflowStatistics, caprock: Dissolved component mass: { { 364.602, 0 }, { 268.637, 215816 } } kg +compflowStatistics: Max phase CFL number: 3.34442 +compflowStatistics: Max component CFL number: 1.57332 +Time: 2.93e+08s, dt:1e+06s, Cycle: 1187 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.417: ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.25e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.53e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00474061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.211704 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76714e+07, 1.77106e+07, 1.77473e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17227e+06, 5.2481e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.522 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.67431, 725.848 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2927.82, 703541 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.357, 213021 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2366.47, 490519 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.741, 0.00107238 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2784.08, 703541 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2927.82, 0 }, { 1167.13, 702350 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76528e+07, 1.76652e+07, 1.76902e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15358e+06, 5.19099e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.8 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.83581, 222.964 } rm^3 +compflowStatistics, caprock: Phase mass: { 366.538, 216085 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 121.027, 65070.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 245.511, 151014 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.76875, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 358.769, 216085 } kg +compflowStatistics, caprock: Dissolved component mass: { { 366.538, 0 }, { 269.238, 215811 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.30883 +compflowStatistics: Max component CFL number: 1.82737 +Time: 2.94e+08s, dt:1e+06s, Cycle: 1188 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.47e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.410: ( Rflow ) = ( 7.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.77e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.77e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0047631 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.147949 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76706e+07, 1.77098e+07, 1.77464e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.17143e+06, 5.24727e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.521 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.66741, 725.854 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2924.62, 703546 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.354, 213021 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2363.27, 490525 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.718, 0.00107237 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2780.91, 703546 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2924.62, 0 }, { 1167.79, 702355 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76519e+07, 1.76644e+07, 1.76893e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15275e+06, 5.19016e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.8 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.840273, 222.96 } rm^3 +compflowStatistics, caprock: Phase mass: { 368.473, 216081 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 121.338, 65070.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 247.135, 151010 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.74627, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 360.727, 216081 } kg +compflowStatistics, caprock: Dissolved component mass: { { 368.473, 0 }, { 269.84, 215806 } } kg +compflowStatistics: Max phase CFL number: 3.24908 +compflowStatistics: Max component CFL number: 1.82821 +Time: 2.95e+08s, dt:1e+06s, Cycle: 1189 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 8.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.78e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.48e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.61e-03 ) ; + Attemptwell_1Control: well is shut +: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.07e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-06 ) ; + Last LinSolve(iter,res) = ( 9, 1.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0047891 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.148964 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76698e+07, 1.77089e+07, 1.77456e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1706e+06, 5.24643e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.521 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.6605, 725.86 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2921.42, 703552 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.362, 213021 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2360.06, 490531 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.713, 0.00107237 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2777.7, 703552 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2921.42, 0 }, { 1168.47, 702361 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76511e+07, 1.76635e+07, 1.76885e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15192e+06, 5.18933e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.8 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.844736, 222.955 } rm^3 +compflowStatistics, caprock: Phase mass: { 370.408, 216076 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 121.645, 65070.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 248.763, 151005 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.64478, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 362.763, 216076 } kg +compflowStatistics, caprock: Dissolved component mass: { { 370.408, 0 }, { 270.44, 215800 } } kg +compflowStatistics: Max phase CFL number: 2.9017 +compflowStatistics: Max component CFL number: 1.97158 +Time: 2.96e+08s, dt:1e+06s, Cycle: 1190 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.19e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.69e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.19e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.78e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.10e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00477895 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.124334 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76689e+07, 1.77081e+07, 1.77448e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16976e+06, 5.24559e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.52 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.6536, 725.867 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2918.21, 703558 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.381, 213021 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2356.83, 490537 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.636, 0.00107236 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2774.58, 703558 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2918.21, 0 }, { 1169.13, 702366 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76502e+07, 1.76627e+07, 1.76877e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15108e+06, 5.18849e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.8 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.849194, 222.95 } rm^3 +compflowStatistics, caprock: Phase mass: { 372.341, 216072 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 121.95, 65070.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 250.391, 151001 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.6329, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 364.708, 216072 } kg +compflowStatistics, caprock: Dissolved component mass: { { 372.341, 0 }, { 271.042, 215795 } } kg +compflowStatistics: Max phase CFL number: 2.75991 +compflowStatistics: Max component CFL number: 1.8826 +Time: 2.97e+08s, dt:1e+06s, Cycle: 1191 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.28e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.67e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00470803 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.192178 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76681e+07, 1.77073e+07, 1.77439e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16892e+06, 5.24475e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.52 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.64674, 725.873 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2915.04, 703564 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.41, 213020 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2353.63, 490543 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.474, 0.00107235 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2771.56, 703564 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2915.04, 0 }, { 1169.78, 702371 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76494e+07, 1.76619e+07, 1.76868e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.15024e+06, 5.18765e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.799 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.853649, 222.946 } rm^3 +compflowStatistics, caprock: Phase mass: { 374.272, 216067 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 122.251, 65070.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 252.021, 150996 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.58787, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 366.684, 216067 } kg +compflowStatistics, caprock: Dissolved component mass: { { 374.272, 0 }, { 271.648, 215790 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.65626 +compflowStatistics: Max component CFL number: 1.69443 +Time: 2.98e+08s, dt:1e+06s, Cycle: 1192 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.31e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00469778 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.188848 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.76673e+07, 1.77064e+07, 1.77431e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1681e+06, 5.24393e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.519 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.63988, 725.879 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2911.86, 703570 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.413, 213020 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2350.44, 490550 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.337, 0.00107235 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2768.52, 703570 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2911.86, 0 }, { 1170.42, 702376 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76486e+07, 1.7661e+07, 1.7686e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14942e+06, 5.18683e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.799 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.858106, 222.941 } rm^3 +compflowStatistics, caprock: Phase mass: { 376.204, 216063 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 122.553, 65070.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 253.651, 150992 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.67507, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 368.529, 216063 } kg +compflowStatistics, caprock: Dissolved component mass: { { 376.204, 0 }, { 272.251, 215785 } } kg +compflowStatistics: Max phase CFL number: 2.83085 +compflowStatistics: Max component CFL number: 1.61415 +Time: 2.99e+08s, dt:1e+06s, Cycle: 1193 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.38e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.24e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.99e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00473095 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.146456 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76664e+07, 1.77056e+07, 1.77423e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16728e+06, 5.24311e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.518 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.63301, 725.885 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2908.67, 703575 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.414, 213020 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2347.26, 490556 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.193, 0.00107234 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2765.48, 703575 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2908.67, 0 }, { 1171.07, 702381 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76478e+07, 1.76602e+07, 1.76852e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14859e+06, 5.186e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.799 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.862557, 222.937 } rm^3 +compflowStatistics, caprock: Phase mass: { 378.133, 216058 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 122.854, 65070.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 255.278, 150988 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.73846, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 370.394, 216058 } kg +compflowStatistics, caprock: Dissolved component mass: { { 378.133, 0 }, { 272.857, 215780 } } kg +compflowStatistics: Max phase CFL number: 4.32861 +compflowStatistics: Max component CFL number: 1.70118 +Time: 3e+08s, dt:1e+06s, Cycle: 1194 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.04e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00471699 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.13591 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76656e+07, 1.77048e+07, 1.77415e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16645e+06, 5.24228e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.518 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.62615, 725.892 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2905.49, 703581 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.417, 213019 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2344.07, 490562 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.136, 0.00107233 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2762.35, 703581 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2905.49, 0 }, { 1171.72, 702386 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76469e+07, 1.76594e+07, 1.76843e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14776e+06, 5.18517e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.799 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.867008, 222.932 } rm^3 +compflowStatistics, caprock: Phase mass: { 380.062, 216054 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 123.153, 65070.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 256.908, 150983 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.76871, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 372.293, 216054 } kg +compflowStatistics, caprock: Dissolved component mass: { { 380.062, 0 }, { 273.46, 215775 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.42481 +compflowStatistics: Max component CFL number: 1.59455 +Time: 3.01e+08s, dt:1e+06s, Cycle: 1195 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.63e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.63e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00463907 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.157904 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76648e+07, 1.7704e+07, 1.77406e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16562e+06, 5.24145e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.517 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.61933, 725.898 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2902.33, 703587 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.446, 213019 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2340.89, 490568 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.061, 0.00107233 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2759.27, 703587 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2902.33, 0 }, { 1172.35, 702391 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76461e+07, 1.76586e+07, 1.76835e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14694e+06, 5.18435e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.799 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.87147, 222.927 } rm^3 +compflowStatistics, caprock: Phase mass: { 381.995, 216049 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 123.454, 65070.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 258.541, 150979 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.66025, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 374.335, 216049 } kg +compflowStatistics, caprock: Dissolved component mass: { { 381.995, 0 }, { 274.055, 215770 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.92863 +compflowStatistics: Max component CFL number: 1.61488 +Time: 3.02e+08s, dt:1e+06s, Cycle: 1196 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.76e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.73e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.54e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0045936 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.145083 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7664e+07, 1.77032e+07, 1.77398e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16481e+06, 5.24064e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.517 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.61252, 725.904 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2899.18, 703593 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.467, 213019 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2337.71, 490574 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.002, 0.00107233 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2756.18, 703593 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2899.18, 0 }, { 1172.97, 702396 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76453e+07, 1.76578e+07, 1.76827e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14613e+06, 5.18354e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.799 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.875935, 222.923 } rm^3 +compflowStatistics, caprock: Phase mass: { 383.93, 216045 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 123.751, 65070.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 260.179, 150974 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.48874, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 376.442, 216045 } kg +compflowStatistics, caprock: Dissolved component mass: { { 383.93, 0 }, { 274.646, 215765 } } kg +compflowStatistics: Max phase CFL number: 3.22551 +compflowStatistics: Max component CFL number: 1.56536 +Time: 3.03e+08s, dt:1e+06s, Cycle: 1197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00458235 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.152974 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76632e+07, 1.77024e+07, 1.7739e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16401e+06, 5.23984e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.516 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.60572, 725.91 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2896.03, 703598 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.486, 213019 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2334.55, 490580 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.959, 0.00107232 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2753.07, 703598 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2896.03, 0 }, { 1173.59, 702401 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76445e+07, 1.7657e+07, 1.76819e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14532e+06, 5.18274e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.798 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.880394, 222.918 } rm^3 +compflowStatistics, caprock: Phase mass: { 385.863, 216040 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 124.044, 65070.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 261.819, 150970 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.41246, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 378.45, 216040 } kg +compflowStatistics, caprock: Dissolved component mass: { { 385.863, 0 }, { 275.241, 215760 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.58975 +compflowStatistics: Max component CFL number: 1.50228 +Time: 3.04e+08s, dt:1e+06s, Cycle: 1198 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.25e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.17e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 8.15e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.15e-07 ) ; + Last LinSolve(iter,res) = ( 8, 1.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00460118 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.136737 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76624e+07, 1.77016e+07, 1.77382e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1632e+06, 5.23904e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.516 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.59891, 725.917 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2892.88, 703604 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.489, 213018 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2331.39, 490586 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.78, 0.00107231 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2750.1, 703604 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2892.88, 0 }, { 1174.22, 702407 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76437e+07, 1.76562e+07, 1.76811e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14452e+06, 5.18193e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.798 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.884853, 222.913 } rm^3 +compflowStatistics, caprock: Phase mass: { 387.795, 216036 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 124.334, 65070.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 263.461, 150965 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.28165, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 380.513, 216036 } kg +compflowStatistics, caprock: Dissolved component mass: { { 387.795, 0 }, { 275.833, 215754 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.55023 +compflowStatistics: Max component CFL number: 1.53533 +Time: 3.05e+08s, dt:1e+06s, Cycle: 1199 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.99e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 6.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.04e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00452171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.146849 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76616e+07, 1.77008e+07, 1.77374e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1624e+06, 5.23823e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.515 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.59215, 725.923 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2889.76, 703610 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.523, 213018 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2328.23, 490592 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.75, 0.00107231 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2747.01, 703610 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2889.76, 0 }, { 1174.83, 702412 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76429e+07, 1.76554e+07, 1.76803e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14371e+06, 5.18113e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.798 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.889315, 222.909 } rm^3 +compflowStatistics, caprock: Phase mass: { 389.728, 216031 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 124.624, 65070.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 265.104, 150961 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.27351, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 382.455, 216031 } kg +compflowStatistics, caprock: Dissolved component mass: { { 389.728, 0 }, { 276.423, 215749 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.71185 +compflowStatistics: Max component CFL number: 1.48271 +Time: 3.06e+08s, dt:1e+06s, Cycle: 1200 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.07e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.07e-06 ) ; + Last LinSolve(iter,res) = ( 9, 9.13e-04 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00445395 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.145224 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76608e+07, 1.77e+07, 1.77367e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16161e+06, 5.23744e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.514 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.58544, 725.929 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2886.65, 703615 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.59, 213018 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2325.06, 490598 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.79, 0.0010723 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2743.86, 703615 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2886.65, 0 }, { 1175.4, 702417 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76421e+07, 1.76546e+07, 1.76796e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14292e+06, 5.18034e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.798 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.893774, 222.904 } rm^3 +compflowStatistics, caprock: Phase mass: { 391.661, 216027 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 124.91, 65070.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 266.751, 150956 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.20592, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 384.455, 216027 } kg +compflowStatistics, caprock: Dissolved component mass: { { 391.661, 0 }, { 277.017, 215744 } } kg +compflowStatistics: Max phase CFL number: 4.68098 +compflowStatistics: Max component CFL number: 1.5296 +Time: 3.07e+08s, dt:1e+06s, Cycle: 1201 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.65e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.95e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.95e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439926 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.12057 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76601e+07, 1.76992e+07, 1.77359e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16083e+06, 5.23667e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.514 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.57875, 725.935 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2883.56, 703621 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.665, 213018 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2321.9, 490604 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.795, 0.00107229 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2740.77, 703621 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2883.56, 0 }, { 1175.97, 702422 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76414e+07, 1.76538e+07, 1.76788e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14214e+06, 5.17956e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.798 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.898229, 222.899 } rm^3 +compflowStatistics, caprock: Phase mass: { 393.591, 216022 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 125.194, 65070.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 268.398, 150952 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.20923, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 386.382, 216022 } kg +compflowStatistics, caprock: Dissolved component mass: { { 393.591, 0 }, { 277.613, 215739 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.637 +compflowStatistics: Max component CFL number: 1.67821 +Time: 3.08e+08s, dt:1e+06s, Cycle: 1202 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.03e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.79e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.53e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.62e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00441273 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.169923 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76593e+07, 1.76985e+07, 1.77351e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.16007e+06, 5.2359e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.513 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.57205, 725.941 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2880.47, 703627 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.719, 213017 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2318.75, 490609 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.699, 0.00107228 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2737.77, 703627 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2880.47, 0 }, { 1176.54, 702427 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76406e+07, 1.76531e+07, 1.7678e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.14137e+06, 5.1788e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.798 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.902681, 222.895 } rm^3 +compflowStatistics, caprock: Phase mass: { 395.52, 216018 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 125.475, 65070.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 270.046, 150947 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.15311, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 388.367, 216018 } kg +compflowStatistics, caprock: Dissolved component mass: { { 395.52, 0 }, { 278.21, 215734 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.84257 +compflowStatistics: Max component CFL number: 1.82457 +Time: 3.09e+08s, dt:1e+06s, Cycle: 1203 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.36e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.27e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.27e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00444527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.174824 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76585e+07, 1.76977e+07, 1.77344e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15929e+06, 5.23513e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.513 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.56533, 725.947 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2877.36, 703632 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.758, 213017 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2315.6, 490615 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.652, 0.00107227 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2734.71, 703632 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2877.36, 0 }, { 1177.12, 702432 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76398e+07, 1.76523e+07, 1.76772e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1406e+06, 5.17803e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.797 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.907133, 222.89 } rm^3 +compflowStatistics, caprock: Phase mass: { 397.449, 216013 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 125.754, 65070.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 271.695, 150943 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.01033, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 390.438, 216013 } kg +compflowStatistics, caprock: Dissolved component mass: { { 397.449, 0 }, { 278.803, 215729 } } kg +compflowStatistics: Max phase CFL number: 4.8021 +compflowStatistics: Max component CFL number: 2.01299 +Time: 3.1e+08s, dt:1e+06s, Cycle: 1204 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.28e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.28e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00442537 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.134057 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76577e+07, 1.76969e+07, 1.77336e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15852e+06, 5.23435e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.512 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.55863, 725.954 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2874.26, 703638 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.771, 213017 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2312.49, 490621 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.453, 0.00107227 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2731.81, 703638 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2874.26, 0 }, { 1177.69, 702437 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76391e+07, 1.76515e+07, 1.76765e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13983e+06, 5.17725e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.797 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.911581, 222.886 } rm^3 +compflowStatistics, caprock: Phase mass: { 399.376, 216009 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 126.032, 65070.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 273.344, 150939 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.05294, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 392.323, 216009 } kg +compflowStatistics, caprock: Dissolved component mass: { { 399.376, 0 }, { 279.397, 215724 } } kg +compflowStatistics: Max phase CFL number: 4.86595 +compflowStatistics: Max component CFL number: 2.20513 +Time: 3.11e+08s, dt:1e+06s, Cycle: 1205 +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.62e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e+00 ) ; + Last LinSolve(iter,res) = ( 4, 5.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.96e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 8.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.23e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.23e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.25e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00444848 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.159006 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7657e+07, 1.76961e+07, 1.77328e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15774e+06, 5.23358e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.512 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.55192, 725.96 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2871.17, 703644 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.777, 213016 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2309.39, 490627 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.329, 0.00107226 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2728.84, 703644 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2871.17, 0 }, { 1178.27, 702442 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76383e+07, 1.76507e+07, 1.76757e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13905e+06, 5.17647e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.797 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.916024, 222.881 } rm^3 +compflowStatistics, caprock: Phase mass: { 401.299, 216004 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 126.307, 65070.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 274.992, 150934 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.1317, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 394.168, 216004 } kg +compflowStatistics, caprock: Dissolved component mass: { { 401.299, 0 }, { 279.994, 215719 } } kg +compflowStatistics: Max phase CFL number: 4.53718 +compflowStatistics: Max component CFL number: 2.04473 +Time: 3.12e+08s, dt:1e+06s, Cycle: 1206 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.98e-03 ) ; + Line search @ 0.464: ( Rflow ) = ( 8.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.70e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.77e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.06e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.31e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00444093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.165729 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76562e+07, 1.76954e+07, 1.7732e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15696e+06, 5.2328e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.511 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.54522, 725.966 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2868.07, 703649 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.783, 213016 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2306.29, 490633 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.245, 0.00107226 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2725.83, 703649 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2868.07, 0 }, { 1178.85, 702447 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76375e+07, 1.76499e+07, 1.76749e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13827e+06, 5.1757e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.797 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.920463, 222.876 } rm^3 +compflowStatistics, caprock: Phase mass: { 403.222, 216000 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 126.578, 65070.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 276.644, 150930 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.87308, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 396.349, 216000 } kg +compflowStatistics, caprock: Dissolved component mass: { { 403.222, 0 }, { 280.591, 215714 } } kg +compflowStatistics: Max phase CFL number: 4.2447 +compflowStatistics: Max component CFL number: 2.00508 +Time: 3.13e+08s, dt:1e+06s, Cycle: 1207 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.17e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e+00 ) ; + Last LinSolve(iter,res) = ( 6, 5.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.92e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.92e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.07e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.03e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.03e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00446768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.148882 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76554e+07, 1.76946e+07, 1.77312e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15619e+06, 5.23202e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.51 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.53852, 725.972 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2864.97, 703655 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.779, 213016 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2303.2, 490639 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.166, 0.00107225 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2722.81, 703655 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2864.97, 0 }, { 1179.43, 702452 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76367e+07, 1.76492e+07, 1.76741e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1375e+06, 5.17492e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.797 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.924895, 222.872 } rm^3 +compflowStatistics, caprock: Phase mass: { 405.141, 215995 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 126.842, 65070.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 278.299, 150925 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.76409, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 398.377, 215995 } kg +compflowStatistics, caprock: Dissolved component mass: { { 405.141, 0 }, { 281.192, 215709 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.02693 +compflowStatistics: Max component CFL number: 1.97844 +Time: 3.14e+08s, dt:1e+06s, Cycle: 1208 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e+00 ) ; + Last LinSolve(iter,res) = ( 4, 9.06e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.53e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.15e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.73e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.73e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.48e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00455211 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.134087 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76546e+07, 1.76938e+07, 1.77304e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15541e+06, 5.23124e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.51 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.53178, 725.978 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2861.86, 703661 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.754, 213016 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2300.11, 490645 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.016, 0.00107225 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2719.84, 703661 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2861.86, 0 }, { 1180.02, 702457 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76359e+07, 1.76484e+07, 1.76733e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13672e+06, 5.17414e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.796 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.929319, 222.867 } rm^3 +compflowStatistics, caprock: Phase mass: { 407.055, 215991 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 127.103, 65070.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 279.952, 150921 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.68501, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 400.37, 215991 } kg +compflowStatistics, caprock: Dissolved component mass: { { 407.055, 0 }, { 281.795, 215704 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.76745 +compflowStatistics: Max component CFL number: 2.07099 +Time: 3.15e+08s, dt:1e+06s, Cycle: 1209 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.43e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00459381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.108546 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76538e+07, 1.7693e+07, 1.77296e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15461e+06, 5.23045e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.509 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.52503, 725.984 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2858.74, 703666 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.741, 213015 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2297, 490651 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.04, 0.00107224 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2716.7, 703666 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2858.74, 0 }, { 1180.63, 702462 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76351e+07, 1.76476e+07, 1.76725e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13593e+06, 5.17334e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.796 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.933735, 222.863 } rm^3 +compflowStatistics, caprock: Phase mass: { 408.966, 215987 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 127.361, 65070.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 281.606, 150917 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.63139, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 402.335, 215987 } kg +compflowStatistics, caprock: Dissolved component mass: { { 408.966, 0 }, { 282.401, 215699 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.9127 +compflowStatistics: Max component CFL number: 1.94062 +Time: 3.16e+08s, dt:1e+06s, Cycle: 1210 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.62e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.62e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.50e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.50e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.79e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00462636 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.140883 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7653e+07, 1.76922e+07, 1.77288e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15381e+06, 5.22965e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.509 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.51826, 725.99 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2855.61, 703672 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.73, 213015 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2293.88, 490657 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.984, 0.00107224 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2713.63, 703672 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2855.61, 0 }, { 1181.24, 702467 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76343e+07, 1.76468e+07, 1.76717e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13513e+06, 5.17254e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.796 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.93815, 222.858 } rm^3 +compflowStatistics, caprock: Phase mass: { 410.876, 215982 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 127.618, 65070 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 283.258, 150912 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.66867, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 404.208, 215982 } kg +compflowStatistics, caprock: Dissolved component mass: { { 410.876, 0 }, { 283.004, 215694 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.95281 +compflowStatistics: Max component CFL number: 1.91046 +Time: 3.17e+08s, dt:1e+06s, Cycle: 1211 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.80e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.80e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.77e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00465604 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.164919 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76522e+07, 1.76914e+07, 1.7728e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.153e+06, 5.22884e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.508 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.51149, 725.997 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2852.48, 703678 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.721, 213015 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2290.76, 490663 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.943, 0.00107225 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2710.54, 703678 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2852.48, 0 }, { 1181.86, 702473 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76335e+07, 1.7646e+07, 1.76709e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13432e+06, 5.17174e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.796 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.942558, 222.853 } rm^3 +compflowStatistics, caprock: Phase mass: { 412.783, 215978 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 127.874, 65070 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 284.909, 150908 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.67057, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 406.112, 215978 } kg +compflowStatistics, caprock: Dissolved component mass: { { 412.783, 0 }, { 283.61, 215688 } } kg +compflowStatistics: Max phase CFL number: 3.6147 +compflowStatistics: Max component CFL number: 1.86117 +Time: 3.18e+08s, dt:1e+06s, Cycle: 1212 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.41e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.41e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00465817 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.145061 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76514e+07, 1.76906e+07, 1.77272e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15219e+06, 5.22803e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.508 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.50473, 726.003 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2849.35, 703683 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.714, 213014 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2287.64, 490669 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.877, 0.00107225 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2707.47, 703683 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2849.35, 0 }, { 1182.47, 702478 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76327e+07, 1.76451e+07, 1.76701e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13351e+06, 5.17092e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.796 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.946958, 222.849 } rm^3 +compflowStatistics, caprock: Phase mass: { 414.685, 215973 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 128.126, 65069.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 286.56, 150903 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.6909, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 407.995, 215973 } kg +compflowStatistics, caprock: Dissolved component mass: { { 414.685, 0 }, { 284.221, 215683 } } kg +compflowStatistics: Max phase CFL number: 3.02578 +compflowStatistics: Max component CFL number: 1.78186 +Time: 3.19e+08s, dt:1e+06s, Cycle: 1213 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.04e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.64e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00466147 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.143336 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76506e+07, 1.76897e+07, 1.77264e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15138e+06, 5.22722e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.507 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.49798, 726.009 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2846.23, 703689 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.722, 213014 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2284.51, 490675 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.897, 0.00107224 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2704.33, 703689 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2846.23, 0 }, { 1183.08, 702483 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76319e+07, 1.76443e+07, 1.76693e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1327e+06, 5.17011e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.796 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.951353, 222.844 } rm^3 +compflowStatistics, caprock: Phase mass: { 416.586, 215969 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 128.377, 65069.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 288.208, 150899 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.73792, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 409.848, 215969 } kg +compflowStatistics, caprock: Dissolved component mass: { { 416.586, 0 }, { 284.834, 215678 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.90022 +compflowStatistics: Max component CFL number: 1.73609 +Time: 3.2e+08s, dt:1e+06s, Cycle: 1214 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.24e-03 ) ; + Line search @ 0.405: ( Rflow ) = ( 5.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.202: ( Rflow ) = ( 9.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.101: ( Rflow ) = ( 8.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e+00 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e+00 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Line search @ 0.456: ( Rflow ) = ( 6.70e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.228: ( Rflow ) = ( 2.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.114: ( Rflow ) = ( 8.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.057: ( Rflow ) = ( 7.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.19e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.19e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.98e-03 ) ; + Line search @ 0.489: ( Rflow ) = ( 1.91e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.244: ( Rflow ) = ( 8.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.122: ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.33e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.93e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.76e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-01 ) ; + Last LinSolve(iter,res) = ( 4, 8.32e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 1.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 8 + ( Rflow ) = ( 2.05e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00463152 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.198781 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76498e+07, 1.76889e+07, 1.77256e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.15057e+06, 5.22641e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.506 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.49124, 726.015 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2843.11, 703695 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.754, 213014 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2281.36, 490681 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.957, 0.00107224 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2701.16, 703695 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2843.11, 0 }, { 1183.69, 702488 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76311e+07, 1.76435e+07, 1.76685e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13189e+06, 5.1693e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.795 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.95575, 222.84 } rm^3 +compflowStatistics, caprock: Phase mass: { 418.487, 215964 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 128.632, 65069.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 289.855, 150895 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.85909, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 411.628, 215964 } kg +compflowStatistics, caprock: Dissolved component mass: { { 418.487, 0 }, { 285.443, 215673 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.85156 +compflowStatistics: Max component CFL number: 1.5285 +Time: 3.21e+08s, dt:1e+06s, Cycle: 1215 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.62e-03 ) ; + Line search @ 0.455: ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.89e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-01 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.27e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.34e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00466023 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.144563 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7649e+07, 1.76881e+07, 1.77248e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14977e+06, 5.22561e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.506 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.4845, 726.021 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2840, 703700 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.797, 213014 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2278.2, 490687 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.864, 0.00107223 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2698.13, 703700 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2840, 0 }, { 1184.3, 702493 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76303e+07, 1.76427e+07, 1.76677e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13109e+06, 5.1685e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.795 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.960143, 222.835 } rm^3 +compflowStatistics, caprock: Phase mass: { 420.386, 215960 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 128.884, 65069.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 291.502, 150890 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.82776, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 413.558, 215960 } kg +compflowStatistics, caprock: Dissolved component mass: { { 420.386, 0 }, { 286.053, 215668 } } kg +compflowStatistics: Max phase CFL number: 2.48562 +compflowStatistics: Max component CFL number: 1.07402 +Time: 3.22e+08s, dt:1e+06s, Cycle: 1216 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.08e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.08e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00467461 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.125637 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76482e+07, 1.76873e+07, 1.7724e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14896e+06, 5.2248e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.505 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.47775, 726.027 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2836.88, 703706 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.821, 213013 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2275.05, 490693 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.859, 0.00107223 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2695.02, 703706 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2836.88, 0 }, { 1184.92, 702498 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76295e+07, 1.76419e+07, 1.76669e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.13028e+06, 5.16769e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.795 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.964542, 222.831 } rm^3 +compflowStatistics, caprock: Phase mass: { 422.288, 215956 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 129.14, 65069.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 293.148, 150886 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.78904, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 415.499, 215956 } kg +compflowStatistics, caprock: Dissolved component mass: { { 422.288, 0 }, { 286.653, 215663 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.30243 +compflowStatistics: Max component CFL number: 0.964662 +Time: 3.23e+08s, dt:1e+06s, Cycle: 1217 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.02e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.90e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.45e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.98e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.64e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.96e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 7.90e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.90e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.68e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00469139 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.132746 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76473e+07, 1.76865e+07, 1.77232e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14815e+06, 5.22399e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.505 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.47099, 726.034 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2833.75, 703712 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.82, 213013 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2271.93, 490699 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.734, 0.00107224 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2692.02, 703712 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2833.75, 0 }, { 1185.54, 702503 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76287e+07, 1.76411e+07, 1.76661e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12948e+06, 5.16689e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.795 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.968943, 222.826 } rm^3 +compflowStatistics, caprock: Phase mass: { 424.19, 215951 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 129.395, 65069.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 294.795, 150881 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.68555, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 417.504, 215951 } kg +compflowStatistics, caprock: Dissolved component mass: { { 424.19, 0 }, { 287.248, 215658 } } kg +compflowStatistics: Max phase CFL number: 2.60676 +compflowStatistics: Max component CFL number: 0.971236 +Time: 3.24e+08s, dt:1e+06s, Cycle: 1218 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-01 ) ; + Last LinSolve(iter,res) = ( 4, 6.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.29e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.21e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0046739 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.119856 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76465e+07, 1.76857e+07, 1.77224e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14734e+06, 5.22318e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.504 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.46423, 726.04 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2830.63, 703718 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.835, 213013 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2268.79, 490705 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.837, 0.00107224 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2688.79, 703718 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2830.63, 0 }, { 1186.17, 702508 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76279e+07, 1.76403e+07, 1.76653e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12867e+06, 5.16608e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.795 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.973341, 222.821 } rm^3 +compflowStatistics, caprock: Phase mass: { 426.09, 215947 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 129.65, 65069.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 296.441, 150877 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.79087, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 419.299, 215947 } kg +compflowStatistics, caprock: Dissolved component mass: { { 426.09, 0 }, { 287.843, 215653 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.92644 +compflowStatistics: Max component CFL number: 1.0032 +Time: 3.25e+08s, dt:1e+06s, Cycle: 1219 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.24e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.39e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.39e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.46e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.46e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.21e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00455729 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.174563 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76457e+07, 1.76849e+07, 1.77216e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14653e+06, 5.22237e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.503 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.45753, 726.046 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2827.54, 703723 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.876, 213013 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2265.66, 490711 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 141.922, 0.00107223 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2685.61, 703723 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2827.54, 0 }, { 1186.77, 702513 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76271e+07, 1.76395e+07, 1.76645e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12786e+06, 5.16527e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.795 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.977735, 222.817 } rm^3 +compflowStatistics, caprock: Phase mass: { 427.99, 215942 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 129.896, 65069.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 298.093, 150873 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.50945, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 421.48, 215942 } kg +compflowStatistics, caprock: Dissolved component mass: { { 427.99, 0 }, { 288.441, 215648 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.07021 +compflowStatistics: Max component CFL number: 0.950823 +Time: 3.26e+08s, dt:1e+06s, Cycle: 1220 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.00e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.00e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.37e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00454064 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.156631 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7645e+07, 1.76841e+07, 1.77208e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14574e+06, 5.22158e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.503 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.45084, 726.052 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2824.44, 703729 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.906, 213012 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2262.54, 490717 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.167, 0.00107222 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2682.28, 703729 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2824.44, 0 }, { 1187.36, 702518 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76263e+07, 1.76387e+07, 1.76637e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12706e+06, 5.16448e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.794 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.982124, 222.812 } rm^3 +compflowStatistics, caprock: Phase mass: { 429.886, 215938 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 130.139, 65069.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 299.748, 150868 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.3144, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 423.572, 215938 } kg +compflowStatistics, caprock: Dissolved component mass: { { 429.886, 0 }, { 289.04, 215643 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.11944 +compflowStatistics: Max component CFL number: 1.09137 +Time: 3.27e+08s, dt:1e+06s, Cycle: 1221 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.94e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.94e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.94e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00451767 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.131756 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76442e+07, 1.76833e+07, 1.772e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14495e+06, 5.22079e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.502 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.44415, 726.058 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2821.36, 703734 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.939, 213012 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2259.42, 490722 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.483, 0.00107222 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2678.87, 703734 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2821.36, 0 }, { 1187.95, 702523 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76255e+07, 1.76379e+07, 1.76629e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12627e+06, 5.16369e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.794 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.986512, 222.808 } rm^3 +compflowStatistics, caprock: Phase mass: { 431.783, 215933 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 130.381, 65069.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 301.402, 150864 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.32469, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 425.458, 215933 } kg +compflowStatistics, caprock: Dissolved component mass: { { 431.783, 0 }, { 289.638, 215638 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.68485 +compflowStatistics: Max component CFL number: 1.1644 +Time: 3.28e+08s, dt:1e+06s, Cycle: 1222 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.38e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.48e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00454623 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.1425 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76434e+07, 1.76825e+07, 1.77192e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14416e+06, 5.22e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.502 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.43745, 726.064 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2818.26, 703740 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.963, 213012 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2256.3, 490728 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 142.78, 0.00107221 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2675.48, 703740 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2818.26, 0 }, { 1188.56, 702528 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76247e+07, 1.76371e+07, 1.76621e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12548e+06, 5.1629e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.794 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.990896, 222.803 } rm^3 +compflowStatistics, caprock: Phase mass: { 433.677, 215929 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 130.62, 65069.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 303.057, 150859 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.20187, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 427.475, 215929 } kg +compflowStatistics, caprock: Dissolved component mass: { { 433.677, 0 }, { 290.235, 215633 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.30853 +compflowStatistics: Max component CFL number: 0.950733 +Time: 3.29e+08s, dt:1e+06s, Cycle: 1223 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.18e-01 ) ; + Last LinSolve(iter,res) = ( 4, 7.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.71e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.71e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00461364 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.151369 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76426e+07, 1.76817e+07, 1.77184e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14337e+06, 5.21921e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.501 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.43073, 726.07 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2815.16, 703746 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.99, 213011 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2253.17, 490734 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.077, 0.00107222 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2672.08, 703746 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2815.16, 0 }, { 1189.17, 702533 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76239e+07, 1.76363e+07, 1.76613e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12469e+06, 5.1621e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.794 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.995269, 222.799 } rm^3 +compflowStatistics, caprock: Phase mass: { 435.565, 215925 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 130.856, 65069.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 304.709, 150855 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.23086, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 429.335, 215925 } kg +compflowStatistics, caprock: Dissolved component mass: { { 435.565, 0 }, { 290.837, 215628 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.00949 +compflowStatistics: Max component CFL number: 0.715201 +Time: 3.3e+08s, dt:1e+06s, Cycle: 1224 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.55e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.05e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.30e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 9.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.90e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.46e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00458689 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.122789 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76418e+07, 1.76809e+07, 1.77176e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14256e+06, 5.2184e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.501 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.42403, 726.077 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2812.06, 703751 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.035, 213011 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2250.03, 490740 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.468, 0.00107222 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2668.59, 703751 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2812.06, 0 }, { 1189.77, 702538 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76231e+07, 1.76355e+07, 1.76605e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12388e+06, 5.16129e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.794 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0.999632, 222.794 } rm^3 +compflowStatistics, caprock: Phase mass: { 437.45, 215920 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 131.088, 65069.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 306.362, 150851 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.21091, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 431.239, 215920 } kg +compflowStatistics, caprock: Dissolved component mass: { { 437.45, 0 }, { 291.445, 215623 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.42411 +compflowStatistics: Max component CFL number: 0.780472 +Time: 3.31e+08s, dt:1e+06s, Cycle: 1225 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 9.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.38e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.12e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.65e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00454021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.122736 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7641e+07, 1.76801e+07, 1.77168e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14175e+06, 5.21759e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.5 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.41735, 726.083 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2808.98, 703757 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.094, 213011 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2246.89, 490746 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.811, 0.00107221 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2665.17, 703757 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2808.98, 0 }, { 1190.37, 702543 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76223e+07, 1.76347e+07, 1.76597e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12308e+06, 5.16049e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.793 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.00399, 222.789 } rm^3 +compflowStatistics, caprock: Phase mass: { 439.331, 215916 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 131.317, 65069.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 308.014, 150846 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.16197, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 433.169, 215916 } kg +compflowStatistics, caprock: Dissolved component mass: { { 439.331, 0 }, { 292.055, 215618 } } kg +compflowStatistics: Max phase CFL number: 3.63586 +compflowStatistics: Max component CFL number: 1.0337 +Time: 3.32e+08s, dt:1e+06s, Cycle: 1226 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.16e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.71e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.37e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.97e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.97e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00449477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.160441 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76402e+07, 1.76794e+07, 1.7716e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14096e+06, 5.2168e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.499 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.41071, 726.089 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2805.91, 703763 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.139, 213011 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2243.77, 490752 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.134, 0.00107221 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2661.78, 703763 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2805.91, 0 }, { 1190.95, 702548 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76215e+07, 1.76339e+07, 1.76589e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12228e+06, 5.15969e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.793 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.00836, 222.785 } rm^3 +compflowStatistics, caprock: Phase mass: { 441.217, 215911 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 131.549, 65069.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 309.668, 150842 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.15394, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 435.063, 215911 } kg +compflowStatistics, caprock: Dissolved component mass: { { 441.217, 0 }, { 292.656, 215613 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.48974 +compflowStatistics: Max component CFL number: 1.26316 +Time: 3.33e+08s, dt:1e+06s, Cycle: 1227 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.06e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.06e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.42e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.63e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.22e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.22e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00450079 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.166973 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76394e+07, 1.76786e+07, 1.77152e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.14017e+06, 5.21601e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.499 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.40404, 726.095 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2802.84, 703768 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.159, 213010 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2240.68, 490758 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.493, 0.0010722 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2658.35, 703768 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2802.84, 0 }, { 1191.54, 702553 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76207e+07, 1.76331e+07, 1.76581e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1215e+06, 5.15891e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.793 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.01272, 222.78 } rm^3 +compflowStatistics, caprock: Phase mass: { 443.101, 215907 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 131.784, 65069.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 311.317, 150838 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.29426, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 436.807, 215907 } kg +compflowStatistics, caprock: Dissolved component mass: { { 443.101, 0 }, { 293.255, 215608 } } kg +compflowStatistics: Max phase CFL number: 2.39697 +compflowStatistics: Max component CFL number: 1.14567 +Time: 3.34e+08s, dt:1e+06s, Cycle: 1228 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.75e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.75e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.62e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.62e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.84e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.84e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.82e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00453338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.122519 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76386e+07, 1.76778e+07, 1.77144e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13938e+06, 5.21522e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.498 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.39737, 726.101 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2799.76, 703774 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.173, 213010 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2237.59, 490764 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.792, 0.00107219 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2654.97, 703774 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2799.76, 0 }, { 1192.14, 702558 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76199e+07, 1.76323e+07, 1.76573e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.12071e+06, 5.15812e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.793 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.01708, 222.776 } rm^3 +compflowStatistics, caprock: Phase mass: { 444.982, 215903 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 132.013, 65069.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 312.97, 150833 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.03008, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 438.952, 215903 } kg +compflowStatistics, caprock: Dissolved component mass: { { 444.982, 0 }, { 293.854, 215603 } } kg +compflowStatistics: Max phase CFL number: 2.59697 +compflowStatistics: Max component CFL number: 0.624606 +Time: 3.35e+08s, dt:1e+06s, Cycle: 1229 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.16e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00452207 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.107937 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76378e+07, 1.7677e+07, 1.77136e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13859e+06, 5.21443e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.498 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.39071, 726.107 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2796.69, 703779 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.182, 213010 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2234.5, 490770 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.133, 0.00107219 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2651.55, 703779 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2796.69, 0 }, { 1192.73, 702563 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76191e+07, 1.76315e+07, 1.76565e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11991e+06, 5.15732e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.793 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.02142, 222.771 } rm^3 +compflowStatistics, caprock: Phase mass: { 446.859, 215898 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 132.232, 65069.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 314.627, 150829 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.70687, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 441.152, 215898 } kg +compflowStatistics, caprock: Dissolved component mass: { { 446.859, 0 }, { 294.459, 215598 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.71739 +compflowStatistics: Max component CFL number: 0.735115 +Time: 3.36e+08s, dt:1e+06s, Cycle: 1230 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.26e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.80e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00450256 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0927494 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7637e+07, 1.76762e+07, 1.77128e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13779e+06, 5.21363e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.497 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.38407, 726.113 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2793.62, 703785 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.198, 213009 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2231.42, 490775 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.513, 0.00107218 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2648.11, 703785 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2793.62, 0 }, { 1193.31, 702568 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76183e+07, 1.76308e+07, 1.76557e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11912e+06, 5.15653e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.793 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.02577, 222.767 } rm^3 +compflowStatistics, caprock: Phase mass: { 448.734, 215894 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 132.448, 65069.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 316.286, 150825 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.70729, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 443.027, 215894 } kg +compflowStatistics, caprock: Dissolved component mass: { { 448.734, 0 }, { 295.065, 215593 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.71106 +compflowStatistics: Max component CFL number: 0.802644 +Time: 3.37e+08s, dt:1e+06s, Cycle: 1231 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.51e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-05 ) ; + Last LinSolve(iter,res) = ( 8, 9.74e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.10754 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76363e+07, 1.76754e+07, 1.77121e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.137e+06, 5.21284e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.497 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.37752, 726.119 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2790.61, 703791 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.259, 213009 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2228.35, 490781 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.007, 0.00107218 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2644.6, 703791 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2790.61, 0 }, { 1193.85, 702573 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76176e+07, 1.763e+07, 1.7655e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11833e+06, 5.15574e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.792 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.03012, 222.762 } rm^3 +compflowStatistics, caprock: Phase mass: { 450.613, 215889 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 132.666, 65069.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 317.948, 150820 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.67288, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 444.94, 215889 } kg +compflowStatistics, caprock: Dissolved component mass: { { 450.613, 0 }, { 295.666, 215588 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.63012 +compflowStatistics: Max component CFL number: 0.85619 +Time: 3.38e+08s, dt:1e+06s, Cycle: 1232 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.13e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.46e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.03e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.18e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.21e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-06 ) ; + Last LinSolve(iter,res) = ( 7, 1.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00432362 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.100704 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76355e+07, 1.76747e+07, 1.77113e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13625e+06, 5.21209e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.496 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.37099, 726.125 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2787.6, 703796 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.332, 213009 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2225.27, 490787 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.407, 0.00107217 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2641.19, 703796 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2787.6, 0 }, { 1194.38, 702578 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.76168e+07, 1.76292e+07, 1.76542e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11757e+06, 5.15499e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.792 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.03447, 222.758 } rm^3 +compflowStatistics, caprock: Phase mass: { 452.491, 215885 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 132.876, 65069.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 319.614, 150816 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.36845, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 447.122, 215885 } kg +compflowStatistics, caprock: Dissolved component mass: { { 452.491, 0 }, { 296.267, 215583 } } kg +compflowStatistics: Max phase CFL number: 2.90108 +compflowStatistics: Max component CFL number: 0.921033 +Time: 3.39e+08s, dt:1e+06s, Cycle: 1233 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.54e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.78e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00430766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.121617 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76347e+07, 1.76739e+07, 1.77106e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1355e+06, 5.21134e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.495 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.36444, 726.131 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2784.58, 703802 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.374, 213009 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2222.21, 490793 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.815, 0.00107217 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2637.77, 703802 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2784.58, 0 }, { 1194.92, 702583 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76161e+07, 1.76285e+07, 1.76535e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11682e+06, 5.15423e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.792 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.03881, 222.753 } rm^3 +compflowStatistics, caprock: Phase mass: { 454.367, 215881 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 133.087, 65069.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 321.28, 150812 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.30752, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 449.059, 215881 } kg +compflowStatistics, caprock: Dissolved component mass: { { 454.367, 0 }, { 296.865, 215578 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.013 +compflowStatistics: Max component CFL number: 0.938543 +Time: 3.4e+08s, dt:1e+06s, Cycle: 1234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.71e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.60e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.60e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00435236 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.132891 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.7634e+07, 1.76732e+07, 1.77098e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13474e+06, 5.21058e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.495 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.35788, 726.137 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2781.56, 703807 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.406, 213008 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2219.15, 490799 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.274, 0.00107217 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2634.29, 703807 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2781.56, 0 }, { 1195.47, 702588 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76153e+07, 1.76277e+07, 1.76527e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11606e+06, 5.15348e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.792 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.04315, 222.749 } rm^3 +compflowStatistics, caprock: Phase mass: { 456.241, 215876 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 133.298, 65069.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 322.943, 150807 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.34612, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 450.895, 215876 } kg +compflowStatistics, caprock: Dissolved component mass: { { 456.241, 0 }, { 297.462, 215573 } } kg +compflowStatistics: Max phase CFL number: 3.0029 +compflowStatistics: Max component CFL number: 0.952591 +Time: 3.41e+08s, dt:1e+06s, Cycle: 1235 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.17e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.24e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.02e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.02e-05 ) ; + Last LinSolve(iter,res) = ( 7, 2.02e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00439822 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.16716 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76332e+07, 1.76724e+07, 1.7709e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13398e+06, 5.20982e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.494 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.35129, 726.143 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2778.53, 703813 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.437, 213008 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2216.09, 490804 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.775, 0.00107216 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2630.75, 703813 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2778.53, 0 }, { 1196.04, 702593 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76145e+07, 1.7627e+07, 1.76519e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1153e+06, 5.15271e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.792 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.04749, 222.744 } rm^3 +compflowStatistics, caprock: Phase mass: { 458.112, 215872 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 133.509, 65069.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 324.603, 150803 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.35281, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 452.76, 215872 } kg +compflowStatistics, caprock: Dissolved component mass: { { 458.112, 0 }, { 298.057, 215568 } } kg +compflowStatistics: Max phase CFL number: 2.69849 +compflowStatistics: Max component CFL number: 0.936218 +Time: 3.42e+08s, dt:1e+06s, Cycle: 1236 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.12e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.87e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0044465 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.144781 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76324e+07, 1.76716e+07, 1.77083e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13321e+06, 5.20905e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.494 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.34469, 726.149 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2775.48, 703818 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.44, 213008 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2213.04, 490810 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.965, 0.00107216 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2627.52, 703818 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2775.48, 0 }, { 1196.61, 702598 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76137e+07, 1.76262e+07, 1.76512e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11453e+06, 5.15194e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.792 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.05182, 222.74 } rm^3 +compflowStatistics, caprock: Phase mass: { 459.98, 215868 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 133.72, 65069 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 326.26, 150799 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.40212, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 454.577, 215868 } kg +compflowStatistics, caprock: Dissolved component mass: { { 459.98, 0 }, { 298.656, 215563 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.42241 +compflowStatistics: Max component CFL number: 0.804883 +Time: 3.43e+08s, dt:1e+06s, Cycle: 1237 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.23e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.23e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.36e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-04 ) ; + Last LinSolve(iter,res) = ( 7, 4.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00437194 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.151238 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76317e+07, 1.76708e+07, 1.77075e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13242e+06, 5.20826e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.493 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.33814, 726.155 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2772.47, 703824 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.462, 213008 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2210, 490816 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.51, 0.00107215 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2623.96, 703824 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2772.47, 0 }, { 1197.17, 702603 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7613e+07, 1.76254e+07, 1.76504e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11375e+06, 5.15116e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.05615, 222.735 } rm^3 +compflowStatistics, caprock: Phase mass: { 461.847, 215863 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 133.93, 65069 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 327.917, 150794 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.44072, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 456.406, 215863 } kg +compflowStatistics, caprock: Dissolved component mass: { { 461.847, 0 }, { 299.253, 215558 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.52259 +compflowStatistics: Max component CFL number: 0.564604 +Time: 3.44e+08s, dt:1e+06s, Cycle: 1238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.01e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.84e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.11e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.11e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.07e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.29e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.64e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.24e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 1.39e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-06 ) ; + Last LinSolve(iter,res) = ( 9, 6.87e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00432491 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.141478 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76309e+07, 1.76701e+07, 1.77067e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13166e+06, 5.2075e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.493 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.33163, 726.161 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2769.47, 703829 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.499, 213007 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2206.97, 490822 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.159, 0.00107215 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2620.31, 703829 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2769.47, 0 }, { 1197.7, 702608 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76122e+07, 1.76247e+07, 1.76496e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11298e+06, 5.1504e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.06047, 222.731 } rm^3 +compflowStatistics, caprock: Phase mass: { 463.712, 215859 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 134.139, 65069 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 329.573, 150790 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.42395, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 458.288, 215859 } kg +compflowStatistics, caprock: Dissolved component mass: { { 463.712, 0 }, { 299.853, 215553 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.56132 +compflowStatistics: Max component CFL number: 0.577198 +Time: 3.45e+08s, dt:1e+06s, Cycle: 1239 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.04e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.04e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.46e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.60e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.81e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.58e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.58e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.04e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 5.15e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.15e-06 ) ; + Last LinSolve(iter,res) = ( 7, 7.97e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00429885 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0909949 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76302e+07, 1.76693e+07, 1.7706e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13091e+06, 5.20675e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.492 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.32512, 726.167 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2766.47, 703835 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.525, 213007 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2203.95, 490828 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.638, 0.00107214 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2616.83, 703835 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2766.47, 0 }, { 1198.23, 702613 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76115e+07, 1.76239e+07, 1.76489e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11223e+06, 5.14964e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.06479, 222.726 } rm^3 +compflowStatistics, caprock: Phase mass: { 465.575, 215855 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 134.348, 65068.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 331.227, 150786 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.43627, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 460.139, 215855 } kg +compflowStatistics, caprock: Dissolved component mass: { { 465.575, 0 }, { 300.454, 215548 } } kg +compflowStatistics: Max phase CFL number: 2.49842 +compflowStatistics: Max component CFL number: 0.601247 +Time: 3.46e+08s, dt:1e+06s, Cycle: 1240 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.34e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.34e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.90e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.90e-05 ) ; + Last LinSolve(iter,res) = ( 8, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00430701 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0901794 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76294e+07, 1.76686e+07, 1.77052e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.13015e+06, 5.20599e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.492 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.31862, 726.173 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2763.48, 703840 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.538, 213007 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2200.94, 490833 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.989, 0.00107214 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2613.49, 703840 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2763.48, 0 }, { 1198.76, 702618 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76107e+07, 1.76231e+07, 1.76481e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11147e+06, 5.14889e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.0691, 222.722 } rm^3 +compflowStatistics, caprock: Phase mass: { 467.434, 215850 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 134.552, 65068.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 332.882, 150781 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.31771, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 462.117, 215850 } kg +compflowStatistics, caprock: Dissolved component mass: { { 467.434, 0 }, { 301.057, 215543 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.5802 +compflowStatistics: Max component CFL number: 0.741068 +Time: 3.47e+08s, dt:1e+06s, Cycle: 1241 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.31e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.07e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.64e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00432169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0888483 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76286e+07, 1.76678e+07, 1.77045e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1294e+06, 5.20524e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.491 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.3121, 726.179 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2760.48, 703846 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.545, 213007 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2197.93, 490839 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.146, 0.00107214 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2610.33, 703846 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2760.48, 0 }, { 1199.3, 702623 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.761e+07, 1.76224e+07, 1.76474e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.11072e+06, 5.14813e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.07341, 222.717 } rm^3 +compflowStatistics, caprock: Phase mass: { 469.293, 215846 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 134.751, 65068.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 334.542, 150777 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.01616, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 464.276, 215846 } kg +compflowStatistics, caprock: Dissolved component mass: { { 469.293, 0 }, { 301.657, 215538 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.89307 +compflowStatistics: Max component CFL number: 0.970453 +Time: 3.48e+08s, dt:1e+06s, Cycle: 1242 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.01e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.55e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.11e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00436524 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.095406 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76279e+07, 1.7667e+07, 1.77037e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12864e+06, 5.20448e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.49 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.30557, 726.185 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2757.47, 703851 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.527, 213006 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2194.94, 490845 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.234, 0.00107213 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2607.24, 703851 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2757.47, 0 }, { 1199.86, 702628 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76092e+07, 1.76216e+07, 1.76466e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10996e+06, 5.14737e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.791 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.07771, 222.713 } rm^3 +compflowStatistics, caprock: Phase mass: { 471.147, 215842 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 134.946, 65068.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 336.2, 150773 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.96432, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 466.182, 215842 } kg +compflowStatistics, caprock: Dissolved component mass: { { 471.147, 0 }, { 302.259, 215533 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.01533 +compflowStatistics: Max component CFL number: 1.13236 +Time: 3.49e+08s, dt:1e+06s, Cycle: 1243 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.73e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.73e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.66e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00438908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0842573 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.76271e+07, 1.76663e+07, 1.77029e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12787e+06, 5.20371e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.49 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.29904, 726.191 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2754.46, 703857 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.503, 213006 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2191.96, 490851 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.336, 0.00107213 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2604.13, 703857 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2754.46, 0 }, { 1200.41, 702633 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76084e+07, 1.76208e+07, 1.76458e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1092e+06, 5.14661e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.082, 222.708 } rm^3 +compflowStatistics, caprock: Phase mass: { 472.997, 215837 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 135.141, 65068.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 337.856, 150768 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.96309, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 468.034, 215837 } kg +compflowStatistics, caprock: Dissolved component mass: { { 472.997, 0 }, { 302.862, 215528 } } kg +compflowStatistics: Max phase CFL number: 4.11806 +compflowStatistics: Max component CFL number: 1.32748 +Time: 3.5e+08s, dt:1e+06s, Cycle: 1244 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.31e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.52e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.36e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00433951 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0904029 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76263e+07, 1.76655e+07, 1.77022e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1271e+06, 5.20294e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.489 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.29254, 726.197 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2751.47, 703862 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.499, 213006 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2188.97, 490856 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.544, 0.00107213 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2600.93, 703862 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2751.47, 0 }, { 1200.95, 702637 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76077e+07, 1.76201e+07, 1.76451e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10843e+06, 5.14584e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.08629, 222.704 } rm^3 +compflowStatistics, caprock: Phase mass: { 474.845, 215833 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 135.332, 65068.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 339.513, 150764 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.84316, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 470.002, 215833 } kg +compflowStatistics, caprock: Dissolved component mass: { { 474.845, 0 }, { 303.469, 215524 } } kg +compflowStatistics: Max phase CFL number: 3.985 +compflowStatistics: Max component CFL number: 1.48252 +Time: 3.51e+08s, dt:1e+06s, Cycle: 1245 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.65e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.09e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00433107 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.109357 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76256e+07, 1.76648e+07, 1.77014e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12634e+06, 5.20218e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.489 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.28604, 726.203 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2748.48, 703868 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.49, 213005 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2185.99, 490862 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.614, 0.00107213 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2597.87, 703868 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2748.48, 0 }, { 1201.49, 702642 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76069e+07, 1.76193e+07, 1.76443e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10766e+06, 5.14508e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.09057, 222.699 } rm^3 +compflowStatistics, caprock: Phase mass: { 476.691, 215829 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 135.521, 65068.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 341.17, 150760 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.73604, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 471.955, 215829 } kg +compflowStatistics, caprock: Dissolved component mass: { { 476.691, 0 }, { 304.075, 215519 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.58119 +compflowStatistics: Max component CFL number: 1.58455 +Time: 3.52e+08s, dt:1e+06s, Cycle: 1246 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.43e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.43e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00437453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.124901 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.76248e+07, 1.7664e+07, 1.77007e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12558e+06, 5.20142e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.488 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.27954, 726.209 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2745.49, 703873 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.46, 213005 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2183.03, 490868 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.68, 0.00107212 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2594.81, 703873 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2745.49, 0 }, { 1202.03, 702647 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76061e+07, 1.76186e+07, 1.76435e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1069e+06, 5.14431e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.09484, 222.695 } rm^3 +compflowStatistics, caprock: Phase mass: { 478.532, 215824 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 135.708, 65068.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 342.824, 150756 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.75472, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 473.777, 215824 } kg +compflowStatistics, caprock: Dissolved component mass: { { 478.532, 0 }, { 304.687, 215514 } } kg +compflowStatistics: Max phase CFL number: 2.83745 +compflowStatistics: Max component CFL number: 1.57468 +Time: 3.53e+08s, dt:1e+06s, Cycle: 1247 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.44e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.52e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.26e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.26e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00435066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.118046 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7624e+07, 1.76632e+07, 1.76999e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12481e+06, 5.20065e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.488 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.27305, 726.215 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2742.5, 703879 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.432, 213005 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2180.07, 490874 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.805, 0.00107212 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2591.69, 703879 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2742.5, 0 }, { 1202.56, 702652 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76054e+07, 1.76178e+07, 1.76428e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10614e+06, 5.14355e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.0991, 222.691 } rm^3 +compflowStatistics, caprock: Phase mass: { 480.369, 215820 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 135.891, 65068.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 344.478, 150751 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.73272, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 475.636, 215820 } kg +compflowStatistics, caprock: Dissolved component mass: { { 480.369, 0 }, { 305.302, 215509 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.81033 +compflowStatistics: Max component CFL number: 1.27909 +Time: 3.54e+08s, dt:1e+06s, Cycle: 1248 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.43e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 9.59e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.59e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439067 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0928528 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76233e+07, 1.76625e+07, 1.76991e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12405e+06, 5.19989e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.487 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.26657, 726.221 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2739.51, 703884 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.403, 213005 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2177.11, 490879 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.968, 0.00107211 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2588.54, 703884 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2739.51, 0 }, { 1203.1, 702657 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76046e+07, 1.7617e+07, 1.7642e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10537e+06, 5.14278e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.79 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.10336, 222.686 } rm^3 +compflowStatistics, caprock: Phase mass: { 482.201, 215816 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 136.072, 65068.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 346.129, 150747 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.71331, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 477.488, 215816 } kg +compflowStatistics, caprock: Dissolved component mass: { { 482.201, 0 }, { 305.921, 215504 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.63002 +compflowStatistics: Max component CFL number: 0.80043 +Time: 3.55e+08s, dt:1e+06s, Cycle: 1249 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.39e-01 ) ; + Last LinSolve(iter,res) = ( 3, 7.59e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.79e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.79e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.58e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439924 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0884909 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76225e+07, 1.76617e+07, 1.76983e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12328e+06, 5.19912e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.487 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.26008, 726.226 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2736.53, 703889 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.382, 213004 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2174.15, 490885 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.058, 0.00107212 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2585.47, 703889 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2736.53, 0 }, { 1203.63, 702662 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76038e+07, 1.76163e+07, 1.76412e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.1046e+06, 5.14201e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.789 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.1076, 222.682 } rm^3 +compflowStatistics, caprock: Phase mass: { 484.03, 215812 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 136.252, 65068.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 347.778, 150743 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.66442, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 479.366, 215812 } kg +compflowStatistics, caprock: Dissolved component mass: { { 484.03, 0 }, { 306.542, 215499 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.73526 +compflowStatistics: Max component CFL number: 0.728836 +Time: 3.56e+08s, dt:1e+06s, Cycle: 1250 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.31e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.31e-01 ) ; + Last LinSolve(iter,res) = ( 3, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.74e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.37e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0044203 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0947633 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76217e+07, 1.76609e+07, 1.76976e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12251e+06, 5.19835e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.486 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.25359, 726.232 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2733.54, 703895 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.352, 213004 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2171.19, 490891 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.103, 0.00107211 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2582.44, 703895 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2733.54, 0 }, { 1204.17, 702667 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76031e+07, 1.76155e+07, 1.76405e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10384e+06, 5.14124e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.789 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.11184, 222.677 } rm^3 +compflowStatistics, caprock: Phase mass: { 485.855, 215807 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 136.429, 65068.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 349.425, 150739 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.69453, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 481.16, 215807 } kg +compflowStatistics, caprock: Dissolved component mass: { { 485.855, 0 }, { 307.167, 215494 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.72573 +compflowStatistics: Max component CFL number: 0.705157 +Time: 3.57e+08s, dt:1e+06s, Cycle: 1251 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.32e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.25e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 4.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 8.62e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.62e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00440044 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.138282 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7621e+07, 1.76601e+07, 1.76968e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12173e+06, 5.19757e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.485 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.24712, 726.238 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2730.56, 703900 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.328, 213004 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2168.23, 490896 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.151, 0.00107211 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2579.41, 703900 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2730.56, 0 }, { 1204.7, 702672 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76023e+07, 1.76147e+07, 1.76397e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10306e+06, 5.14047e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.789 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.11607, 222.673 } rm^3 +compflowStatistics, caprock: Phase mass: { 487.675, 215803 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 136.605, 65068.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 351.07, 150734 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.71349, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 482.962, 215803 } kg +compflowStatistics, caprock: Dissolved component mass: { { 487.675, 0 }, { 307.796, 215489 } } kg +compflowStatistics: Max phase CFL number: 4.35865 +compflowStatistics: Max component CFL number: 0.969511 +Time: 3.58e+08s, dt:1e+06s, Cycle: 1252 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.72e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.72e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.49e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440833 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.144433 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76202e+07, 1.76594e+07, 1.7696e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12096e+06, 5.1968e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.485 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.24065, 726.244 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2727.58, 703906 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.307, 213004 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2165.27, 490902 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.243, 0.0010721 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2576.34, 703906 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2727.58, 0 }, { 1205.23, 702677 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76015e+07, 1.76139e+07, 1.76389e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10229e+06, 5.13969e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.789 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.12029, 222.669 } rm^3 +compflowStatistics, caprock: Phase mass: { 489.492, 215799 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 136.778, 65068.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 352.714, 150730 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.65493, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 484.837, 215799 } kg +compflowStatistics, caprock: Dissolved component mass: { { 489.492, 0 }, { 308.427, 215484 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.39634 +compflowStatistics: Max component CFL number: 1.04839 +Time: 3.59e+08s, dt:1e+06s, Cycle: 1253 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.14e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00442941 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.119073 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76194e+07, 1.76586e+07, 1.76952e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.12019e+06, 5.19602e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.484 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.23418, 726.25 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2724.6, 703911 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.282, 213003 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2162.32, 490908 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.341, 0.0010721 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2573.26, 703911 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2724.6, 0 }, { 1205.77, 702682 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76007e+07, 1.76132e+07, 1.76381e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10152e+06, 5.13892e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.789 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.1245, 222.664 } rm^3 +compflowStatistics, caprock: Phase mass: { 491.304, 215795 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 136.948, 65068.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 354.356, 150726 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.58137, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 486.723, 215795 } kg +compflowStatistics, caprock: Dissolved component mass: { { 491.304, 0 }, { 309.063, 215479 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.75034 +compflowStatistics: Max component CFL number: 1.12044 +Time: 3.6e+08s, dt:1e+06s, Cycle: 1254 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.38e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.09e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.09e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.49e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.81e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00444755 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.121285 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76186e+07, 1.76578e+07, 1.76945e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11941e+06, 5.19525e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.484 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.22771, 726.256 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2721.62, 703917 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.248, 213003 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2159.37, 490914 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.386, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2570.24, 703917 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2721.62, 0 }, { 1206.3, 702686 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.76e+07, 1.76124e+07, 1.76374e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.10074e+06, 5.13814e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.788 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.1287, 222.66 } rm^3 +compflowStatistics, caprock: Phase mass: { 493.112, 215790 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 137.118, 65068.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 355.993, 150722 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.66652, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 488.445, 215790 } kg +compflowStatistics, caprock: Dissolved component mass: { { 493.112, 0 }, { 309.702, 215475 } } kg +compflowStatistics: Max phase CFL number: 4.78326 +compflowStatistics: Max component CFL number: 1.21682 +Time: 3.61e+08s, dt:1e+06s, Cycle: 1255 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.74e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.40e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.40e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 8.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 9.66e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 7.21e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 8.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.82e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 9.29e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 7 + ( Rflow ) = ( 3.56e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.56e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.43e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00445251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.10937 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76178e+07, 1.7657e+07, 1.76937e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11863e+06, 5.19447e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.483 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.22125, 726.262 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2718.64, 703922 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.211, 213003 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2156.43, 490919 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.363, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2567.28, 703922 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2718.64, 0 }, { 1206.83, 702691 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75992e+07, 1.76116e+07, 1.76366e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09996e+06, 5.13736e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.788 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.13289, 222.655 } rm^3 +compflowStatistics, caprock: Phase mass: { 494.916, 215786 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 137.288, 65068.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 357.628, 150718 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.69988, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 490.216, 215786 } kg +compflowStatistics, caprock: Dissolved component mass: { { 494.916, 0 }, { 310.344, 215470 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 4.76642 +compflowStatistics: Max component CFL number: 1.30485 +Time: 3.62e+08s, dt:1e+06s, Cycle: 1256 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.05e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.05e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.49e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.49e-03 ) ; + Last LinSolve(iter,res) = ( 7, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.16e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00442747 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.125684 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76171e+07, 1.76562e+07, 1.76929e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11785e+06, 5.19369e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.483 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.2148, 726.268 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2715.68, 703927 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.18, 213002 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2153.5, 490925 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.478, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2564.2, 703927 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2715.68, 0 }, { 1207.35, 702696 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75984e+07, 1.76108e+07, 1.76358e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09918e+06, 5.13658e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.788 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.13709, 222.651 } rm^3 +compflowStatistics, caprock: Phase mass: { 496.72, 215782 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 137.456, 65068.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 359.263, 150714 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.5603, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 492.159, 215782 } kg +compflowStatistics, caprock: Dissolved component mass: { { 496.72, 0 }, { 310.983, 215465 } } kg +compflowStatistics: Max phase CFL number: 4.50072 +compflowStatistics: Max component CFL number: 1.3411 +Time: 3.63e+08s, dt:1e+06s, Cycle: 1257 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.98e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.98e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.56e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.83e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.83e-07 ) ; + Last LinSolve(iter,res) = ( 7, 2.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00444967 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.117369 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76163e+07, 1.76555e+07, 1.76921e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11707e+06, 5.19291e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.482 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.20834, 726.274 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2712.7, 703933 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.137, 213002 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2150.57, 490931 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.468, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2561.23, 703933 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2712.7, 0 }, { 1207.89, 702701 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75976e+07, 1.761e+07, 1.7635e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0984e+06, 5.1358e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.788 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.14127, 222.647 } rm^3 +compflowStatistics, caprock: Phase mass: { 498.52, 215778 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 137.625, 65068.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 360.895, 150709 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.64548, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 493.874, 215778 } kg +compflowStatistics, caprock: Dissolved component mass: { { 498.52, 0 }, { 311.624, 215460 } } kg +compflowStatistics: Max phase CFL number: 3.6094 +compflowStatistics: Max component CFL number: 1.27998 +Time: 3.64e+08s, dt:1e+06s, Cycle: 1258 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.82e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.59e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.59e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.53e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.53e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.77e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00443468 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0908126 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76155e+07, 1.76547e+07, 1.76913e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11629e+06, 5.19213e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.481 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.2019, 726.28 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2709.74, 703938 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.096, 213002 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2147.64, 490936 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.48, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2558.26, 703938 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2709.74, 0 }, { 1208.41, 702706 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75968e+07, 1.76093e+07, 1.76342e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09762e+06, 5.13502e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.788 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.14545, 222.642 } rm^3 +compflowStatistics, caprock: Phase mass: { 500.319, 215773 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 137.796, 65068.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 362.523, 150705 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.68743, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 495.631, 215773 } kg +compflowStatistics, caprock: Dissolved component mass: { { 500.319, 0 }, { 312.263, 215455 } } kg +compflowStatistics: Max phase CFL number: 3.04016 +compflowStatistics: Max component CFL number: 0.98881 +Time: 3.65e+08s, dt:1e+06s, Cycle: 1259 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.37e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 3.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440912 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.115636 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76147e+07, 1.76539e+07, 1.76906e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11551e+06, 5.19135e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.481 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.19548, 726.285 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2706.78, 703944 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.059, 213002 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2144.72, 490942 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.569, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2555.21, 703944 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2706.78, 0 }, { 1208.94, 702711 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75961e+07, 1.76085e+07, 1.76335e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09684e+06, 5.13424e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.788 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.14963, 222.638 } rm^3 +compflowStatistics, caprock: Phase mass: { 502.117, 215769 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 137.969, 65068.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 364.148, 150701 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.7585, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 497.358, 215769 } kg +compflowStatistics, caprock: Dissolved component mass: { { 502.117, 0 }, { 312.9, 215450 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.8074 +compflowStatistics: Max component CFL number: 0.709209 +Time: 3.66e+08s, dt:1e+06s, Cycle: 1260 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.20e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.20e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.82e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.66e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.79e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.62e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.70e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.06e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440672 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.145945 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7614e+07, 1.76531e+07, 1.76898e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11474e+06, 5.19058e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.48 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.18906, 726.291 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2703.83, 703949 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 562.017, 213001 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2141.81, 490948 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.608, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2552.22, 703949 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2703.83, 0 }, { 1209.45, 702716 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75953e+07, 1.76077e+07, 1.76327e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09607e+06, 5.13347e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.787 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.1538, 222.634 } rm^3 +compflowStatistics, caprock: Phase mass: { 503.91, 215765 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 138.141, 65068.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 365.769, 150697 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.81495, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 499.095, 215765 } kg +compflowStatistics, caprock: Dissolved component mass: { { 503.91, 0 }, { 313.541, 215445 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.09675 +compflowStatistics: Max component CFL number: 0.660451 +Time: 3.67e+08s, dt:1e+06s, Cycle: 1261 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.08e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.64e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.64e-01 ) ; + Last LinSolve(iter,res) = ( 4, 3.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.15e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.15e-05 ) ; + Last LinSolve(iter,res) = ( 6, 7.24e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0044049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.103722 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76132e+07, 1.76524e+07, 1.7689e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11396e+06, 5.1898e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.48 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.18265, 726.297 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2700.88, 703954 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.967, 213001 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2138.91, 490953 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.623, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2549.25, 703954 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2700.88, 0 }, { 1209.97, 702720 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75945e+07, 1.76069e+07, 1.76319e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0953e+06, 5.1327e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.787 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.15797, 222.629 } rm^3 +compflowStatistics, caprock: Phase mass: { 505.7, 215761 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 138.31, 65068.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 367.39, 150693 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.86309, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 500.837, 215761 } kg +compflowStatistics, caprock: Dissolved component mass: { { 505.7, 0 }, { 314.186, 215441 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.63699 +compflowStatistics: Max component CFL number: 0.593076 +Time: 3.68e+08s, dt:1e+06s, Cycle: 1262 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.25e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.25e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.29e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.86e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.09e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.03e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 4.54e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.54e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0043916 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.14094 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76124e+07, 1.76516e+07, 1.76883e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11319e+06, 5.18903e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.479 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.17625, 726.303 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2697.93, 703960 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.915, 213001 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2136.02, 490959 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.642, 0.00107205 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2546.29, 703960 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2697.93, 0 }, { 1210.48, 702725 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75938e+07, 1.76062e+07, 1.76312e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09452e+06, 5.13192e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.787 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.16213, 222.625 } rm^3 +compflowStatistics, caprock: Phase mass: { 507.488, 215757 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 138.471, 65068.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 369.017, 150689 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.4118, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 503.077, 215757 } kg +compflowStatistics, caprock: Dissolved component mass: { { 507.488, 0 }, { 314.829, 215436 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.61635 +compflowStatistics: Max component CFL number: 0.599577 +Time: 3.69e+08s, dt:1e+06s, Cycle: 1263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.83e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 8.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.79e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.79e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.95e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.21e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.71e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.71e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.37e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 6 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.55e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00442313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0980994 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76116e+07, 1.76508e+07, 1.76875e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11242e+06, 5.18826e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.479 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.16985, 726.309 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2694.98, 703965 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.858, 213001 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2133.13, 490964 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.739, 0.00107205 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2543.25, 703965 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2694.98, 0 }, { 1211, 702730 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7593e+07, 1.76054e+07, 1.76304e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09375e+06, 5.13115e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.787 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.16628, 222.621 } rm^3 +compflowStatistics, caprock: Phase mass: { 509.274, 215752 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 138.629, 65068.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 370.645, 150684 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.16964, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 505.104, 215752 } kg +compflowStatistics, caprock: Dissolved component mass: { { 509.274, 0 }, { 315.472, 215431 } } kg +compflowStatistics: Max phase CFL number: 1.496 +compflowStatistics: Max component CFL number: 0.605226 +Time: 3.7e+08s, dt:1e+06s, Cycle: 1264 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.89e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.06e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00447106 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0870181 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76109e+07, 1.765e+07, 1.76867e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11164e+06, 5.18748e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.478 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.16342, 726.315 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2692.03, 703970 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.795, 213000 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2130.23, 490970 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.824, 0.00107205 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2540.21, 703970 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2692.03, 0 }, { 1211.53, 702735 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75922e+07, 1.76046e+07, 1.76296e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09298e+06, 5.13038e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.787 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.17042, 222.616 } rm^3 +compflowStatistics, caprock: Phase mass: { 511.053, 215748 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 138.784, 65068.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 372.27, 150680 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.22827, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 506.825, 215748 } kg +compflowStatistics, caprock: Dissolved component mass: { { 511.053, 0 }, { 316.121, 215426 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.76682 +compflowStatistics: Max component CFL number: 0.609759 +Time: 3.71e+08s, dt:1e+06s, Cycle: 1265 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-01 ) ; + Last LinSolve(iter,res) = ( 3, 8.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.13e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.52e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 3.25e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 5.30e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.30e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00446595 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0775067 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76101e+07, 1.76493e+07, 1.76859e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11086e+06, 5.1867e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.478 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.15701, 726.32 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2689.08, 703976 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.733, 213000 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2127.34, 490976 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.898, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2537.18, 703976 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2689.08, 0 }, { 1212.05, 702740 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75914e+07, 1.76038e+07, 1.76288e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0922e+06, 5.12959e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.787 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.17455, 222.612 } rm^3 +compflowStatistics, caprock: Phase mass: { 512.829, 215744 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 138.936, 65068 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 373.892, 150676 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.16015, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 508.669, 215744 } kg +compflowStatistics, caprock: Dissolved component mass: { { 512.829, 0 }, { 316.773, 215421 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.15481 +compflowStatistics: Max component CFL number: 0.612046 +Time: 3.72e+08s, dt:1e+06s, Cycle: 1266 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.52e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.52e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.99e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00443082 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0825251 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76093e+07, 1.76485e+07, 1.76851e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.11007e+06, 5.18591e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.477 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.15063, 726.326 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2686.14, 703981 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.685, 213000 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2124.46, 490981 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.924, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2534.22, 703981 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2686.14, 0 }, { 1212.56, 702745 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75906e+07, 1.7603e+07, 1.7628e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09141e+06, 5.12881e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.786 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.17868, 222.608 } rm^3 +compflowStatistics, caprock: Phase mass: { 514.602, 215740 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.089, 65068 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 375.512, 150672 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.15768, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 510.444, 215740 } kg +compflowStatistics, caprock: Dissolved component mass: { { 514.602, 0 }, { 317.427, 215416 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.20899 +compflowStatistics: Max component CFL number: 0.613894 +Time: 3.73e+08s, dt:1e+06s, Cycle: 1267 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.81e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.65e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.69e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.69e-05 ) ; + Last LinSolve(iter,res) = ( 6, 9.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00442883 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.113059 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76085e+07, 1.76477e+07, 1.76844e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1093e+06, 5.18514e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.476 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.14426, 726.332 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2683.21, 703986 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.633, 212999 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2121.57, 490987 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.957, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2531.25, 703986 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2683.21, 0 }, { 1213.07, 702749 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75899e+07, 1.76023e+07, 1.76273e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.09064e+06, 5.12803e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.786 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.1828, 222.603 } rm^3 +compflowStatistics, caprock: Phase mass: { 516.371, 215736 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.239, 65068 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 377.131, 150668 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.11216, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 512.258, 215736 } kg +compflowStatistics, caprock: Dissolved component mass: { { 516.371, 0 }, { 318.084, 215412 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.20992 +compflowStatistics: Max component CFL number: 0.615841 +Time: 3.74e+08s, dt:1e+06s, Cycle: 1268 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.86e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.95e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.95e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00444027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.114086 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76077e+07, 1.76469e+07, 1.76836e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10852e+06, 5.18436e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.476 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.13788, 726.338 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2680.27, 703992 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.574, 212999 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2118.7, 490993 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.96, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2528.31, 703992 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2680.27, 0 }, { 1213.58, 702754 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75891e+07, 1.76015e+07, 1.76265e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08986e+06, 5.12726e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.786 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.18691, 222.599 } rm^3 +compflowStatistics, caprock: Phase mass: { 518.137, 215732 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.387, 65067.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 378.749, 150664 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.00799, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 514.129, 215732 } kg +compflowStatistics, caprock: Dissolved component mass: { { 518.137, 0 }, { 318.741, 215407 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.26118 +compflowStatistics: Max component CFL number: 0.616295 +Time: 3.75e+08s, dt:1e+06s, Cycle: 1269 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.00e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.69e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.69e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.31e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00441207 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0941809 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7607e+07, 1.76461e+07, 1.76828e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10774e+06, 5.18358e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.475 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.13153, 726.344 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2677.35, 703997 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.517, 212999 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2115.83, 490998 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.988, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2525.36, 703997 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2677.35, 0 }, { 1214.08, 702759 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75883e+07, 1.76007e+07, 1.76257e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08908e+06, 5.12648e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.786 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.19102, 222.595 } rm^3 +compflowStatistics, caprock: Phase mass: { 519.9, 215728 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.537, 65067.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 380.363, 150660 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.08405, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 515.816, 215728 } kg +compflowStatistics, caprock: Dissolved component mass: { { 519.9, 0 }, { 319.4, 215402 } } kg +compflowStatistics: Max phase CFL number: 3.14247 +compflowStatistics: Max component CFL number: 0.620567 +Time: 3.76e+08s, dt:1e+06s, Cycle: 1270 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.76e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439579 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0881315 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.76062e+07, 1.76454e+07, 1.7682e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10697e+06, 5.18281e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.475 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.12519, 726.349 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2674.44, 704002 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.467, 212999 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2112.97, 491004 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.128, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2522.31, 704002 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2674.44, 0 }, { 1214.57, 702764 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75875e+07, 1.75999e+07, 1.76249e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08831e+06, 5.1257e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.786 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.19511, 222.591 } rm^3 +compflowStatistics, caprock: Phase mass: { 521.661, 215723 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.688, 65067.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 381.973, 150656 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.17503, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 517.486, 215723 } kg +compflowStatistics, caprock: Dissolved component mass: { { 521.661, 0 }, { 320.062, 215397 } } kg +compflowStatistics: Max phase CFL number: 3.70257 +compflowStatistics: Max component CFL number: 0.792605 +Time: 3.77e+08s, dt:1e+06s, Cycle: 1271 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.81e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.98e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439672 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.099209 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76054e+07, 1.76446e+07, 1.76813e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1062e+06, 5.18204e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.474 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.11886, 726.355 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2671.53, 704008 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.416, 212998 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2110.11, 491009 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.188, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2519.34, 704008 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2671.53, 0 }, { 1215.06, 702769 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75868e+07, 1.75992e+07, 1.76242e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08753e+06, 5.12493e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.786 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.19921, 222.586 } rm^3 +compflowStatistics, caprock: Phase mass: { 523.417, 215719 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.837, 65067.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 383.58, 150652 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.131, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 519.286, 215719 } kg +compflowStatistics, caprock: Dissolved component mass: { { 523.417, 0 }, { 320.726, 215392 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.83097 +compflowStatistics: Max component CFL number: 0.927483 +Time: 3.78e+08s, dt:1e+06s, Cycle: 1272 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.85e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.46e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.79e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00438103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.106044 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76047e+07, 1.76438e+07, 1.76805e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10543e+06, 5.18127e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.474 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.11255, 726.361 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2668.62, 704013 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.366, 212998 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2107.26, 491015 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.238, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2516.38, 704013 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2668.62, 0 }, { 1215.55, 702773 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7586e+07, 1.75984e+07, 1.76234e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08676e+06, 5.12416e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.785 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.20329, 222.582 } rm^3 +compflowStatistics, caprock: Phase mass: { 525.171, 215715 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 139.979, 65067.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 385.191, 150647 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.8916, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 521.279, 215715 } kg +compflowStatistics, caprock: Dissolved component mass: { { 525.171, 0 }, { 321.393, 215388 } } kg +compflowStatistics: Max phase CFL number: 3.74599 +compflowStatistics: Max component CFL number: 0.990028 +Time: 3.79e+08s, dt:1e+06s, Cycle: 1273 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.08e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.24e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.19e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.19e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.87e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00437076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.107004 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76039e+07, 1.76431e+07, 1.76797e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10466e+06, 5.1805e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.473 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.10625, 726.367 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2665.72, 704018 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.324, 212998 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2104.4, 491020 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.447, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2513.28, 704018 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2665.72, 0 }, { 1216.03, 702778 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75852e+07, 1.75976e+07, 1.76226e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.086e+06, 5.12339e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.785 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.20736, 222.578 } rm^3 +compflowStatistics, caprock: Phase mass: { 526.92, 215711 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.121, 65067.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 386.8, 150643 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.8877, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 523.033, 215711 } kg +compflowStatistics, caprock: Dissolved component mass: { { 526.92, 0 }, { 322.062, 215383 } } kg +compflowStatistics: Max phase CFL number: 3.92281 +compflowStatistics: Max component CFL number: 1.18918 +Time: 3.8e+08s, dt:1e+06s, Cycle: 1274 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.80e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.55e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.14e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0043746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0867207 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76031e+07, 1.76423e+07, 1.7679e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10389e+06, 5.17973e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.472 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.09995, 726.372 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2662.83, 704023 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.277, 212998 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2101.55, 491026 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.523, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2510.31, 704023 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2662.83, 0 }, { 1216.5, 702783 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75845e+07, 1.75969e+07, 1.76219e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08523e+06, 5.12263e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.785 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.21143, 222.574 } rm^3 +compflowStatistics, caprock: Phase mass: { 528.666, 215707 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.259, 65067.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 388.407, 150639 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.77478, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 524.891, 215707 } kg +compflowStatistics, caprock: Dissolved component mass: { { 528.666, 0 }, { 322.735, 215378 } } kg +compflowStatistics: Max phase CFL number: 4.01143 +compflowStatistics: Max component CFL number: 1.45187 +Time: 3.81e+08s, dt:1e+06s, Cycle: 1275 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.84e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.09e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.70e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.19e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0044073 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.102936 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76024e+07, 1.76415e+07, 1.76782e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10313e+06, 5.17896e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.472 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.09366, 726.378 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2659.93, 704029 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.226, 212997 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2098.71, 491031 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.725, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2507.21, 704029 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2659.93, 0 }, { 1216.98, 702788 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75837e+07, 1.75961e+07, 1.76211e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08446e+06, 5.12186e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.785 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.21549, 222.569 } rm^3 +compflowStatistics, caprock: Phase mass: { 530.407, 215703 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.398, 65067.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 390.009, 150635 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.86322, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 526.543, 215703 } kg +compflowStatistics, caprock: Dissolved component mass: { { 530.407, 0 }, { 323.412, 215373 } } kg +compflowStatistics: Max phase CFL number: 3.92931 +compflowStatistics: Max component CFL number: 1.71154 +Time: 3.82e+08s, dt:1e+06s, Cycle: 1276 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.22e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.22e-01 ) ; + Last LinSolve(iter,res) = ( 3, 9.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.65e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.50e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00443035 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0996108 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76016e+07, 1.76408e+07, 1.76774e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10235e+06, 5.17819e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.471 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.08735, 726.384 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2657.03, 704034 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.156, 212997 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2095.88, 491037 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.702, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2504.33, 704034 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2657.03, 0 }, { 1217.46, 702792 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75829e+07, 1.75953e+07, 1.76203e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08369e+06, 5.12109e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.785 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.21954, 222.565 } rm^3 +compflowStatistics, caprock: Phase mass: { 532.144, 215699 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.534, 65067.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 391.61, 150631 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.76911, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 528.375, 215699 } kg +compflowStatistics, caprock: Dissolved component mass: { { 532.144, 0 }, { 324.089, 215369 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.65301 +compflowStatistics: Max component CFL number: 1.91053 +Time: 3.83e+08s, dt:1e+06s, Cycle: 1277 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.38e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.38e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.33e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.98e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440946 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0876972 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76008e+07, 1.764e+07, 1.76766e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10158e+06, 5.17742e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.471 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.08106, 726.39 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2654.14, 704039 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 561.072, 212997 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2093.07, 491042 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.766, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2501.38, 704039 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2654.14, 0 }, { 1217.94, 702797 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75821e+07, 1.75946e+07, 1.76195e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08292e+06, 5.12031e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.785 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.22358, 222.561 } rm^3 +compflowStatistics, caprock: Phase mass: { 533.879, 215695 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.668, 65067.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 393.211, 150627 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.68005, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 530.199, 215695 } kg +compflowStatistics, caprock: Dissolved component mass: { { 533.879, 0 }, { 324.767, 215364 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.368 +compflowStatistics: Max component CFL number: 2.11531 +Time: 3.84e+08s, dt:1e+06s, Cycle: 1278 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.13e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.13e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.03e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00438882 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0768061 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.76e+07, 1.76392e+07, 1.76759e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.1008e+06, 5.17664e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.47 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.07479, 726.395 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2651.26, 704044 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.99, 212996 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2090.27, 491048 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.76, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2498.5, 704044 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2651.26, 0 }, { 1218.42, 702802 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75814e+07, 1.75938e+07, 1.76188e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08214e+06, 5.11954e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.22762, 222.557 } rm^3 +compflowStatistics, caprock: Phase mass: { 535.612, 215691 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.802, 65067.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 394.81, 150623 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.57411, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 532.038, 215691 } kg +compflowStatistics, caprock: Dissolved component mass: { { 535.612, 0 }, { 325.443, 215359 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.03046 +compflowStatistics: Max component CFL number: 2.27696 +Time: 3.85e+08s, dt:1e+06s, Cycle: 1279 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.76e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.42e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00435804 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.119242 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75993e+07, 1.76385e+07, 1.76751e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.10003e+06, 5.17587e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.47 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.06854, 726.401 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2648.39, 704050 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.919, 212996 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2087.47, 491053 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.773, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2495.61, 704050 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2648.39, 0 }, { 1218.88, 702807 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75806e+07, 1.7593e+07, 1.7618e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08137e+06, 5.11877e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.23166, 222.553 } rm^3 +compflowStatistics, caprock: Phase mass: { 537.345, 215687 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 140.935, 65067.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 396.41, 150619 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.44154, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 533.903, 215687 } kg +compflowStatistics, caprock: Dissolved component mass: { { 537.345, 0 }, { 326.118, 215354 } } kg +compflowStatistics: Max phase CFL number: 2.5795 +compflowStatistics: Max component CFL number: 2.3266 +Time: 3.86e+08s, dt:1e+06s, Cycle: 1280 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.84e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.84e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.92e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 9.44e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.44e-05 ) ; + Last LinSolve(iter,res) = ( 7, 6.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00433302 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.130457 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75985e+07, 1.76377e+07, 1.76744e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09927e+06, 5.17511e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.469 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.06231, 726.407 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2645.52, 704055 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.846, 212996 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2084.68, 491059 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.709, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2492.81, 704055 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2645.52, 0 }, { 1219.34, 702811 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75799e+07, 1.75923e+07, 1.76173e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.08061e+06, 5.11801e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.23569, 222.548 } rm^3 +compflowStatistics, caprock: Phase mass: { 539.076, 215683 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.069, 65067.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 398.007, 150615 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.50124, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 535.574, 215683 } kg +compflowStatistics, caprock: Dissolved component mass: { { 539.076, 0 }, { 326.792, 215350 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.06246 +compflowStatistics: Max component CFL number: 2.27362 +Time: 3.87e+08s, dt:1e+06s, Cycle: 1281 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.07e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.43e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.43e-07 ) ; + Last LinSolve(iter,res) = ( 9, 1.12e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0043301 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.114671 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75978e+07, 1.76369e+07, 1.76736e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09852e+06, 5.17435e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.469 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.05608, 726.412 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2642.66, 704060 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.777, 212996 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2081.88, 491064 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.681, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2489.98, 704060 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2642.66, 0 }, { 1219.8, 702816 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75791e+07, 1.75915e+07, 1.76165e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07985e+06, 5.11725e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.23972, 222.544 } rm^3 +compflowStatistics, caprock: Phase mass: { 540.803, 215679 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.202, 65067.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 399.601, 150611 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.43994, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 537.363, 215679 } kg +compflowStatistics, caprock: Dissolved component mass: { { 540.803, 0 }, { 327.469, 215345 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.58894 +compflowStatistics: Max component CFL number: 2.02523 +Time: 3.88e+08s, dt:1e+06s, Cycle: 1282 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.24e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 9.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 6.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.56e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.56e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00433141 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0833885 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7597e+07, 1.76362e+07, 1.76728e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09776e+06, 5.1736e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.468 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.04986, 726.418 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2639.8, 704065 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.711, 212995 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2079.09, 491070 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.665, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2487.14, 704065 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2639.8, 0 }, { 1220.26, 702821 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75783e+07, 1.75907e+07, 1.76157e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0791e+06, 5.11649e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.24374, 222.54 } rm^3 +compflowStatistics, caprock: Phase mass: { 542.525, 215675 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.334, 65067.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 401.192, 150607 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.4622, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 539.063, 215675 } kg +compflowStatistics, caprock: Dissolved component mass: { { 542.525, 0 }, { 328.15, 215340 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.35362 +compflowStatistics: Max component CFL number: 1.61128 +Time: 3.89e+08s, dt:1e+06s, Cycle: 1283 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.10e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00434423 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0772364 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75962e+07, 1.76354e+07, 1.76721e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.097e+06, 5.17284e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.467 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.04364, 726.424 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2636.94, 704070 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.641, 212995 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2076.3, 491075 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.442, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2484.5, 704070 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2636.94, 0 }, { 1220.71, 702826 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75776e+07, 1.759e+07, 1.7615e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07834e+06, 5.11573e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.784 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.24775, 222.536 } rm^3 +compflowStatistics, caprock: Phase mass: { 544.244, 215671 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.464, 65067.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 402.781, 150603 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.33876, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 540.906, 215671 } kg +compflowStatistics, caprock: Dissolved component mass: { { 544.244, 0 }, { 328.831, 215335 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.40797 +compflowStatistics: Max component CFL number: 1.15479 +Time: 3.9e+08s, dt:1e+06s, Cycle: 1284 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.72e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.39e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.38e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0043618 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0757432 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75955e+07, 1.76346e+07, 1.76713e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09624e+06, 5.17208e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.467 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.03741, 726.429 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2634.08, 704076 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.556, 212995 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2073.53, 491081 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.304, 0.0010721 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2481.78, 704076 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2634.08, 0 }, { 1221.17, 702830 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75768e+07, 1.75892e+07, 1.76142e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07758e+06, 5.11497e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.783 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.25175, 222.532 } rm^3 +compflowStatistics, caprock: Phase mass: { 545.96, 215667 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.594, 65067.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 404.366, 150599 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.3429, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 542.617, 215667 } kg +compflowStatistics, caprock: Dissolved component mass: { { 545.96, 0 }, { 329.514, 215331 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.45715 +compflowStatistics: Max component CFL number: 0.806588 +Time: 3.91e+08s, dt:1e+06s, Cycle: 1285 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.32e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.56e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.56e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00434925 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659735 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75947e+07, 1.76339e+07, 1.76705e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09547e+06, 5.17131e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.466 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.0312, 726.435 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2631.23, 704081 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.468, 212995 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2070.76, 491086 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.205, 0.0010721 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2479.02, 704081 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2631.23, 0 }, { 1221.63, 702835 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7576e+07, 1.75885e+07, 1.76134e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07681e+06, 5.11421e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.783 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.25575, 222.527 } rm^3 +compflowStatistics, caprock: Phase mass: { 547.673, 215663 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.723, 65067.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 405.95, 150595 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.26, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 544.413, 215663 } kg +compflowStatistics, caprock: Dissolved component mass: { { 547.673, 0 }, { 330.198, 215326 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.48935 +compflowStatistics: Max component CFL number: 0.732383 +Time: 3.92e+08s, dt:1e+06s, Cycle: 1286 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.97e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.97e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.38e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.38e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.53e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00434319 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683344 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75939e+07, 1.76331e+07, 1.76698e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09471e+06, 5.17055e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.466 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.025, 726.441 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2628.38, 704086 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.384, 212994 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2068, 491092 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.114, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2476.27, 704086 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2628.38, 0 }, { 1222.08, 702840 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75753e+07, 1.75877e+07, 1.76127e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07605e+06, 5.11344e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.783 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.25973, 222.523 } rm^3 +compflowStatistics, caprock: Phase mass: { 549.382, 215659 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.85, 65067.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 407.532, 150591 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.26997, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 546.112, 215659 } kg +compflowStatistics, caprock: Dissolved component mass: { { 549.382, 0 }, { 330.885, 215321 } } kg +compflowStatistics: Max phase CFL number: 1.49999 +compflowStatistics: Max component CFL number: 0.706485 +Time: 3.93e+08s, dt:1e+06s, Cycle: 1287 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.78e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00437671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0698344 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75932e+07, 1.76324e+07, 1.7669e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09395e+06, 5.16979e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.465 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.0188, 726.446 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2625.53, 704091 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.297, 212994 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2065.23, 491097 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 152.035, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2473.49, 704091 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2625.53, 0 }, { 1222.54, 702844 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75745e+07, 1.75869e+07, 1.76119e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07529e+06, 5.11268e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.783 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.26371, 222.519 } rm^3 +compflowStatistics, caprock: Phase mass: { 551.085, 215655 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 141.973, 65067.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 409.113, 150587 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.09969, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 547.986, 215655 } kg +compflowStatistics, caprock: Dissolved component mass: { { 551.085, 0 }, { 331.576, 215317 } } kg +compflowStatistics: Max phase CFL number: 1.48558 +compflowStatistics: Max component CFL number: 0.70254 +Time: 3.94e+08s, dt:1e+06s, Cycle: 1288 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-02 ) ; +well_1Control: well is shut + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.96e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.06984 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75924e+07, 1.76316e+07, 1.76682e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09318e+06, 5.16902e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.465 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.01259, 726.452 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2622.68, 704096 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.208, 212994 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2062.47, 491103 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.916, 0.0010721 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2470.76, 704096 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2622.68, 0 }, { 1223, 702849 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75737e+07, 1.75862e+07, 1.76111e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07452e+06, 5.11191e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.783 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.26767, 222.515 } rm^3 +compflowStatistics, caprock: Phase mass: { 552.783, 215651 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.094, 65067.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 410.689, 150583 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.15335, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 549.63, 215651 } kg +compflowStatistics, caprock: Dissolved component mass: { { 552.783, 0 }, { 332.272, 215312 } } kg +compflowStatistics: Max phase CFL number: 1.427 +compflowStatistics: Max component CFL number: 0.666688 +Time: 3.95e+08s, dt:1e+06s, Cycle: 1289 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.27e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.28e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00443167 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664442 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75916e+07, 1.76308e+07, 1.76675e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09241e+06, 5.16824e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.464 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.00638, 726.458 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2619.82, 704101 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.116, 212993 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2059.7, 491108 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.851, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2467.97, 704101 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2619.82, 0 }, { 1223.46, 702854 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7573e+07, 1.75854e+07, 1.76104e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07375e+06, 5.11114e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.27163, 222.511 } rm^3 +compflowStatistics, caprock: Phase mass: { 554.476, 215647 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.214, 65067.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 412.262, 150579 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.12152, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 551.354, 215647 } kg +compflowStatistics, caprock: Dissolved component mass: { { 554.476, 0 }, { 332.972, 215307 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.28577 +compflowStatistics: Max component CFL number: 0.658877 +Time: 3.96e+08s, dt:1e+06s, Cycle: 1290 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.30e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.30e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.29e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00445326 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0650584 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75908e+07, 1.763e+07, 1.76667e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09163e+06, 5.16747e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.464 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 6.00017, 726.463 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2616.96, 704107 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 560.019, 212993 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2056.95, 491113 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.669, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2465.3, 704107 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2616.96, 0 }, { 1223.93, 702858 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75722e+07, 1.75846e+07, 1.76096e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07297e+06, 5.11036e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.27557, 222.507 } rm^3 +compflowStatistics, caprock: Phase mass: { 556.164, 215643 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.333, 65067.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 413.831, 150575 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.16935, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 552.995, 215643 } kg +compflowStatistics, caprock: Dissolved component mass: { { 556.164, 0 }, { 333.676, 215303 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.83985 +compflowStatistics: Max component CFL number: 0.671553 +Time: 3.97e+08s, dt:1e+06s, Cycle: 1291 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.18e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.11e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.11e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.55e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00447527 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0810242 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75901e+07, 1.76292e+07, 1.76659e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09085e+06, 5.16669e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.463 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.99396, 726.469 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2614.11, 704112 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.912, 212993 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2054.2, 491119 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.482, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2462.63, 704112 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2614.11, 0 }, { 1224.39, 702863 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75714e+07, 1.75838e+07, 1.76088e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07219e+06, 5.10958e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.2795, 222.503 } rm^3 +compflowStatistics, caprock: Phase mass: { 557.848, 215639 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.451, 65067.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 415.396, 150572 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.14183, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 554.706, 215639 } kg +compflowStatistics, caprock: Dissolved component mass: { { 557.848, 0 }, { 334.382, 215298 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.03061 +compflowStatistics: Max component CFL number: 0.642919 +Time: 3.98e+08s, dt:1e+06s, Cycle: 1292 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.42e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.17e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.26e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.26e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.65e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.55e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 7.78e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.78e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00446449 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.101194 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75893e+07, 1.76285e+07, 1.76651e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.09006e+06, 5.1659e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.462 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.98776, 726.475 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2611.26, 704117 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.801, 212993 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2051.46, 491124 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 151.218, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2460.04, 704117 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2611.26, 0 }, { 1224.86, 702868 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75706e+07, 1.7583e+07, 1.7608e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07141e+06, 5.1088e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.28343, 222.499 } rm^3 +compflowStatistics, caprock: Phase mass: { 559.529, 215635 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.571, 65067.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 416.958, 150568 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.16828, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 556.36, 215635 } kg +compflowStatistics, caprock: Dissolved component mass: { { 559.529, 0 }, { 335.088, 215293 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.11429 +compflowStatistics: Max component CFL number: 0.629503 +Time: 3.99e+08s, dt:1e+06s, Cycle: 1293 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.46e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.46e-03 ) ; + Last LinSolve(iter,res) = ( 6, 9.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.38e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.38e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.82e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00447103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.110827 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75885e+07, 1.76277e+07, 1.76643e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08928e+06, 5.16512e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.462 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.98156, 726.48 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2608.41, 704122 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.679, 212992 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2048.73, 491130 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.978, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2457.43, 704122 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2608.41, 0 }, { 1225.32, 702872 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75698e+07, 1.75822e+07, 1.76072e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.07063e+06, 5.10801e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.28735, 222.494 } rm^3 +compflowStatistics, caprock: Phase mass: { 561.206, 215631 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.69, 65067.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 418.516, 150564 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.12703, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 558.079, 215631 } kg +compflowStatistics, caprock: Dissolved component mass: { { 561.206, 0 }, { 335.798, 215289 } } kg +compflowStatistics: Max phase CFL number: 2.12073 +compflowStatistics: Max component CFL number: 0.610489 +Time: 4e+08s, dt:1e+06s, Cycle: 1294 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.99e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.99e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00447668 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.115063 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75877e+07, 1.76269e+07, 1.76635e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08849e+06, 5.16433e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.461 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.97537, 726.486 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2605.56, 704127 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.554, 212992 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2046.01, 491135 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.849, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2454.71, 704127 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2605.56, 0 }, { 1225.78, 702877 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75691e+07, 1.75815e+07, 1.76064e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06984e+06, 5.10723e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.782 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.29126, 222.49 } rm^3 +compflowStatistics, caprock: Phase mass: { 562.879, 215627 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.809, 65067.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 420.07, 150560 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.16074, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 559.718, 215627 } kg +compflowStatistics, caprock: Dissolved component mass: { { 562.879, 0 }, { 336.509, 215284 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.97387 +compflowStatistics: Max component CFL number: 0.592585 +Time: 4.01e+08s, dt:1e+06s, Cycle: 1295 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.06e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.06e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.14e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.14e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00448266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.10426 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75869e+07, 1.76261e+07, 1.76628e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08771e+06, 5.16355e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.461 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.96919, 726.491 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2602.72, 704132 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.433, 212992 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2043.28, 491140 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.725, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2451.99, 704132 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2602.72, 0 }, { 1226.24, 702882 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75683e+07, 1.75807e+07, 1.76057e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06906e+06, 5.10644e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.781 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.29516, 222.486 } rm^3 +compflowStatistics, caprock: Phase mass: { 564.547, 215623 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 142.927, 65067.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 421.62, 150556 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.21026, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 561.337, 215623 } kg +compflowStatistics, caprock: Dissolved component mass: { { 564.547, 0 }, { 337.225, 215279 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.686 +compflowStatistics: Max component CFL number: 0.582179 +Time: 4.02e+08s, dt:1e+06s, Cycle: 1296 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.60e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.89e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-05 ) ; + Last LinSolve(iter,res) = ( 6, 2.41e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00449446 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0795701 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75861e+07, 1.76253e+07, 1.7662e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08692e+06, 5.16276e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.46 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.96301, 726.497 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2599.88, 704137 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.314, 212992 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2040.56, 491146 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.587, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2449.29, 704137 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2599.88, 0 }, { 1226.7, 702886 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75675e+07, 1.75799e+07, 1.76049e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06827e+06, 5.10566e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.781 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.29906, 222.482 } rm^3 +compflowStatistics, caprock: Phase mass: { 566.211, 215619 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.045, 65067 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 423.166, 150552 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.25264, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 562.958, 215619 } kg +compflowStatistics, caprock: Dissolved component mass: { { 566.211, 0 }, { 337.945, 215275 } } kg +compflowStatistics: Max phase CFL number: 1.50639 +compflowStatistics: Max component CFL number: 0.585482 +Time: 4.03e+08s, dt:1e+06s, Cycle: 1297 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.27e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00449848 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657199 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75853e+07, 1.76245e+07, 1.76612e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08613e+06, 5.16197e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.46 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.95684, 726.503 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2597.04, 704142 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.193, 212991 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2037.84, 491151 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.477, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2446.56, 704142 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2597.04, 0 }, { 1227.16, 702891 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75667e+07, 1.75791e+07, 1.76041e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06749e+06, 5.10487e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.781 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.30294, 222.478 } rm^3 +compflowStatistics, caprock: Phase mass: { 567.871, 215615 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.163, 65067 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 424.709, 150548 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.21916, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 564.652, 215615 } kg +compflowStatistics, caprock: Dissolved component mass: { { 567.871, 0 }, { 338.664, 215270 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.39981 +compflowStatistics: Max component CFL number: 0.58954 +Time: 4.04e+08s, dt:1e+06s, Cycle: 1298 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00448814 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685233 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75846e+07, 1.76237e+07, 1.76604e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08534e+06, 5.16118e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.459 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.95067, 726.508 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2594.2, 704148 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 559.074, 212991 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2035.13, 491157 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.391, 0.00107209 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2443.81, 704148 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2594.2, 0 }, { 1227.62, 702896 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75659e+07, 1.75783e+07, 1.76033e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0667e+06, 5.10408e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.781 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.30682, 222.474 } rm^3 +compflowStatistics, caprock: Phase mass: { 569.53, 215611 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.281, 65067 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 426.249, 150544 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.21786, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 566.312, 215611 } kg +compflowStatistics, caprock: Dissolved component mass: { { 569.53, 0 }, { 339.384, 215265 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.76949 +compflowStatistics: Max component CFL number: 0.590379 +Time: 4.05e+08s, dt:1e+06s, Cycle: 1299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.19e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.19e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.85e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.85e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00451013 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0781582 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75838e+07, 1.76229e+07, 1.76596e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08456e+06, 5.1604e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.458 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.94451, 726.514 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2591.37, 704153 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.954, 212991 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2032.41, 491162 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.236, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2441.13, 704153 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2591.37, 0 }, { 1228.08, 702900 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75651e+07, 1.75775e+07, 1.76025e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06591e+06, 5.10329e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.781 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.31069, 222.47 } rm^3 +compflowStatistics, caprock: Phase mass: { 571.185, 215607 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.401, 65066.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 427.784, 150540 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.27231, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 567.912, 215607 } kg +compflowStatistics, caprock: Dissolved component mass: { { 571.185, 0 }, { 340.105, 215261 } } kg +compflowStatistics: Max phase CFL number: 2.91322 +compflowStatistics: Max component CFL number: 0.665882 +Time: 4.06e+08s, dt:1e+06s, Cycle: 1300 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.80e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.80e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00450164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0855634 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7583e+07, 1.76222e+07, 1.76588e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08377e+06, 5.15961e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.458 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.93835, 726.519 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2588.54, 704158 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.838, 212990 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2029.7, 491167 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 150.12, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2438.42, 704158 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2588.54, 0 }, { 1228.53, 702905 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75643e+07, 1.75767e+07, 1.76017e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06512e+06, 5.1025e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.781 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.31456, 222.466 } rm^3 +compflowStatistics, caprock: Phase mass: { 572.836, 215604 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.521, 65066.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 429.315, 150537 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.27169, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 569.565, 215604 } kg +compflowStatistics, caprock: Dissolved component mass: { { 572.836, 0 }, { 340.828, 215256 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.89373 +compflowStatistics: Max component CFL number: 0.735321 +Time: 4.07e+08s, dt:1e+06s, Cycle: 1301 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.03e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.03e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.39e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0044956 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0895332 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75822e+07, 1.76214e+07, 1.7658e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08298e+06, 5.15882e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.457 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.93221, 726.525 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2585.71, 704163 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.727, 212990 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2026.99, 491173 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.991, 0.00107208 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2435.72, 704163 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2585.71, 0 }, { 1228.98, 702910 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75635e+07, 1.75759e+07, 1.76009e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06433e+06, 5.10171e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.78 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.31841, 222.462 } rm^3 +compflowStatistics, caprock: Phase mass: { 574.484, 215600 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.641, 65066.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 430.843, 150533 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.33495, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 571.149, 215600 } kg +compflowStatistics, caprock: Dissolved component mass: { { 574.484, 0 }, { 341.554, 215251 } } kg +compflowStatistics: Max phase CFL number: 2.89954 +compflowStatistics: Max component CFL number: 0.753991 +Time: 4.08e+08s, dt:1e+06s, Cycle: 1302 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.68e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.87e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.87e-06 ) ; + Last LinSolve(iter,res) = ( 4, 8.72e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00448513 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0830086 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75814e+07, 1.76206e+07, 1.76572e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08219e+06, 5.15803e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.457 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.92608, 726.531 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2582.9, 704168 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.62, 212990 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2024.28, 491178 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.876, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2433.02, 704168 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2582.9, 0 }, { 1229.43, 702914 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75628e+07, 1.75752e+07, 1.76001e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06354e+06, 5.10093e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.78 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.32226, 222.458 } rm^3 +compflowStatistics, caprock: Phase mass: { 576.129, 215596 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.76, 65066.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 432.369, 150529 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.27976, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 572.849, 215596 } kg +compflowStatistics, caprock: Dissolved component mass: { { 576.129, 0 }, { 342.28, 215247 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.86555 +compflowStatistics: Max component CFL number: 0.657524 +Time: 4.09e+08s, dt:1e+06s, Cycle: 1303 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.41e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.41e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.26e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.26e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.82e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00451405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641696 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75806e+07, 1.76198e+07, 1.76565e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0814e+06, 5.15724e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.456 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.91995, 726.536 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2580.08, 704173 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.51, 212990 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2021.57, 491183 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.752, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2430.32, 704173 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2580.08, 0 }, { 1229.88, 702919 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7562e+07, 1.75744e+07, 1.75994e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06276e+06, 5.10014e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.78 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.3261, 222.454 } rm^3 +compflowStatistics, caprock: Phase mass: { 577.769, 215592 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.876, 65066.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 433.894, 150525 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.12713, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 574.642, 215592 } kg +compflowStatistics, caprock: Dissolved component mass: { { 577.769, 0 }, { 343.008, 215242 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.97123 +compflowStatistics: Max component CFL number: 0.593667 +Time: 4.1e+08s, dt:1e+06s, Cycle: 1304 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.78e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.84e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.84e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.57e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.87e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00452313 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0880115 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75798e+07, 1.7619e+07, 1.76557e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.08061e+06, 5.15645e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.456 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.91382, 726.542 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2577.26, 704178 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.401, 212989 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2018.86, 491189 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.619, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2427.64, 704178 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2577.26, 0 }, { 1230.33, 702923 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75612e+07, 1.75736e+07, 1.75986e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06197e+06, 5.09935e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.78 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.32994, 222.45 } rm^3 +compflowStatistics, caprock: Phase mass: { 579.406, 215588 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 143.989, 65066.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 435.417, 150521 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.04695, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 576.359, 215588 } kg +compflowStatistics, caprock: Dissolved component mass: { { 579.406, 0 }, { 343.739, 215238 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.11872 +compflowStatistics: Max component CFL number: 0.651944 +Time: 4.11e+08s, dt:1e+06s, Cycle: 1305 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.63e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.63e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.29e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.29e-05 ) ; + Last LinSolve(iter,res) = ( 7, 8.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00450883 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0846255 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7579e+07, 1.76182e+07, 1.76549e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07982e+06, 5.15566e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.455 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.9077, 726.547 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2574.45, 704183 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.288, 212989 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2016.16, 491194 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.464, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2424.98, 704183 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2574.45, 0 }, { 1230.78, 702928 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75604e+07, 1.75728e+07, 1.75978e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06118e+06, 5.09856e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.78 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.33377, 222.446 } rm^3 +compflowStatistics, caprock: Phase mass: { 581.043, 215584 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.105, 65066.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 436.938, 150517 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 2.96303, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 578.08, 215584 } kg +compflowStatistics, caprock: Dissolved component mass: { { 581.043, 0 }, { 344.466, 215233 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.25497 +compflowStatistics: Max component CFL number: 0.722976 +Time: 4.12e+08s, dt:1e+06s, Cycle: 1306 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.52e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.48e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.48e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.70e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00451417 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672645 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75782e+07, 1.76174e+07, 1.76541e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07903e+06, 5.15487e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.454 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.90159, 726.553 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2571.64, 704188 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.172, 212989 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2013.46, 491199 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.357, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2422.28, 704188 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2571.64, 0 }, { 1231.23, 702933 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75596e+07, 1.7572e+07, 1.7597e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.06039e+06, 5.09777e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.78 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.33759, 222.442 } rm^3 +compflowStatistics, caprock: Phase mass: { 582.676, 215580 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.222, 65066.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 438.454, 150514 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.05405, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 579.622, 215580 } kg +compflowStatistics, caprock: Dissolved component mass: { { 582.676, 0 }, { 345.193, 215228 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.36893 +compflowStatistics: Max component CFL number: 0.793625 +Time: 4.13e+08s, dt:1e+06s, Cycle: 1307 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.16e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.16e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.32e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.32e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.10e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.52e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 9.99e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.99e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 2.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.30e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00451506 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722524 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75775e+07, 1.76166e+07, 1.76533e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07825e+06, 5.15409e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.454 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.89548, 726.558 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2568.83, 704193 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 558.059, 212988 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2010.77, 491205 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.184, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2419.65, 704193 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2568.83, 0 }, { 1231.67, 702937 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75588e+07, 1.75712e+07, 1.75962e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0596e+06, 5.09698e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.779 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.34141, 222.438 } rm^3 +compflowStatistics, caprock: Phase mass: { 584.306, 215577 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.341, 65066.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 439.965, 150510 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.15523, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 581.15, 215577 } kg +compflowStatistics, caprock: Dissolved component mass: { { 584.306, 0 }, { 345.923, 215224 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.35403 +compflowStatistics: Max component CFL number: 0.815402 +Time: 4.14e+08s, dt:1e+06s, Cycle: 1308 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.05e-03 ) ; + Last LinSolve(iter,res) = ( 7, 7.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.42e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.42e-07 ) ; + Last LinSolve(iter,res) = ( 10, 5.53e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00452554 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701109 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75767e+07, 1.76158e+07, 1.76525e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07746e+06, 5.1533e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.453 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.88938, 726.564 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2566.03, 704198 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.946, 212988 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2008.08, 491210 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 149.067, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2416.96, 704198 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2566.03, 0 }, { 1232.12, 702942 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7558e+07, 1.75704e+07, 1.75954e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05881e+06, 5.09619e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.779 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.34522, 222.434 } rm^3 +compflowStatistics, caprock: Phase mass: { 585.931, 215573 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.459, 65066.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 441.472, 150506 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.13566, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 582.796, 215573 } kg +compflowStatistics, caprock: Dissolved component mass: { { 585.931, 0 }, { 346.655, 215219 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.35852 +compflowStatistics: Max component CFL number: 0.845127 +Time: 4.15e+08s, dt:1e+06s, Cycle: 1309 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.80e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.69e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0045248 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649066 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75759e+07, 1.76151e+07, 1.76517e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07667e+06, 5.15251e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.453 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.88329, 726.569 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2563.23, 704203 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.834, 212988 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2005.39, 491215 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.896, 0.00107207 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2414.33, 704203 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2563.23, 0 }, { 1232.56, 702946 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75572e+07, 1.75696e+07, 1.75946e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05802e+06, 5.09541e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.779 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.34902, 222.43 } rm^3 +compflowStatistics, caprock: Phase mass: { 587.554, 215569 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.574, 65066.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 442.98, 150502 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.02704, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 584.527, 215569 } kg +compflowStatistics, caprock: Dissolved component mass: { { 587.554, 0 }, { 347.388, 215215 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.32719 +compflowStatistics: Max component CFL number: 0.866563 +Time: 4.16e+08s, dt:1e+06s, Cycle: 1310 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.02e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.02e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.78e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0045276 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070025 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75751e+07, 1.76143e+07, 1.76509e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07588e+06, 5.15172e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.452 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.87721, 726.575 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2560.43, 704208 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.721, 212988 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2002.71, 491221 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.763, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2411.67, 704208 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2560.43, 0 }, { 1233.01, 702951 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75564e+07, 1.75688e+07, 1.75938e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05724e+06, 5.09462e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.779 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.35282, 222.426 } rm^3 +compflowStatistics, caprock: Phase mass: { 589.175, 215565 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.691, 65066.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 444.484, 150498 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 2.98133, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 586.193, 215565 } kg +compflowStatistics, caprock: Dissolved component mass: { { 589.175, 0 }, { 348.119, 215210 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.24285 +compflowStatistics: Max component CFL number: 0.874902 +Time: 4.17e+08s, dt:1e+06s, Cycle: 1311 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.55e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.55e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.22e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00450505 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728952 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75743e+07, 1.76135e+07, 1.76501e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07509e+06, 5.15093e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.452 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.87114, 726.58 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2557.64, 704213 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.619, 212987 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 2000.02, 491226 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.677, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2408.97, 704213 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2557.64, 0 }, { 1233.44, 702955 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75557e+07, 1.75681e+07, 1.7593e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05645e+06, 5.09383e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.779 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.35661, 222.422 } rm^3 +compflowStatistics, caprock: Phase mass: { 590.792, 215561 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.809, 65066.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 445.984, 150495 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.04313, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 587.749, 215561 } kg +compflowStatistics, caprock: Dissolved component mass: { { 590.792, 0 }, { 348.853, 215206 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.08106 +compflowStatistics: Max component CFL number: 0.869197 +Time: 4.18e+08s, dt:1e+06s, Cycle: 1312 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.15e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.15e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.90e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00450546 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0726845 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75735e+07, 1.76127e+07, 1.76494e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07431e+06, 5.15015e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.451 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.86508, 726.586 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2554.86, 704218 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.512, 212987 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1997.35, 491231 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.504, 0.00107206 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2406.36, 704218 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2554.86, 0 }, { 1233.88, 702960 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75549e+07, 1.75673e+07, 1.75923e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05566e+06, 5.09304e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.778 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.36039, 222.418 } rm^3 +compflowStatistics, caprock: Phase mass: { 592.406, 215557 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 144.926, 65066.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 447.48, 150491 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.03522, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 589.371, 215557 } kg +compflowStatistics, caprock: Dissolved component mass: { { 592.406, 0 }, { 349.589, 215201 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.7794 +compflowStatistics: Max component CFL number: 0.837693 +Time: 4.19e+08s, dt:1e+06s, Cycle: 1313 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.40e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.40e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.94e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00449519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682744 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75727e+07, 1.76119e+07, 1.76486e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07352e+06, 5.14936e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.45 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.85904, 726.591 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2552.08, 704223 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.406, 212987 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1994.68, 491236 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.406, 0.00107205 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2403.68, 704223 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2552.08, 0 }, { 1234.31, 702965 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75541e+07, 1.75665e+07, 1.75915e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05488e+06, 5.09226e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.778 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.36417, 222.414 } rm^3 +compflowStatistics, caprock: Phase mass: { 594.016, 215554 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.044, 65066.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 448.972, 150487 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.08253, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 590.934, 215554 } kg +compflowStatistics, caprock: Dissolved component mass: { { 594.016, 0 }, { 350.326, 215196 } } kg +compflowStatistics: Max phase CFL number: 2.2418 +compflowStatistics: Max component CFL number: 0.759161 +Time: 4.2e+08s, dt:1e+06s, Cycle: 1314 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.09e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.76e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00447051 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665896 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.7572e+07, 1.76111e+07, 1.76478e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07274e+06, 5.14858e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.45 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.85301, 726.597 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2549.31, 704228 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.307, 212986 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1992.01, 491242 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.315, 0.00107205 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2401, 704228 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2549.31, 0 }, { 1234.73, 702969 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75533e+07, 1.75657e+07, 1.75907e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05409e+06, 5.09148e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.778 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.36794, 222.41 } rm^3 +compflowStatistics, caprock: Phase mass: { 595.623, 215550 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.162, 65066.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 450.461, 150483 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.06801, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 592.555, 215550 } kg +compflowStatistics, caprock: Dissolved component mass: { { 595.623, 0 }, { 351.066, 215192 } } kg +compflowStatistics: Max phase CFL number: 2.13735 +compflowStatistics: Max component CFL number: 0.60827 +Time: 4.21e+08s, dt:1e+06s, Cycle: 1315 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.22e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.39e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-06 ) ; + Last LinSolve(iter,res) = ( 6, 2.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00447714 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679061 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75712e+07, 1.76104e+07, 1.7647e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07196e+06, 5.1478e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.449 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.84699, 726.602 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2546.55, 704233 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.204, 212986 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1989.34, 491247 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 148.14, 0.00107205 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2398.41, 704233 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2546.55, 0 }, { 1235.15, 702974 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75525e+07, 1.75649e+07, 1.75899e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05332e+06, 5.0907e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.778 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.37169, 222.406 } rm^3 +compflowStatistics, caprock: Phase mass: { 597.226, 215546 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.279, 65066.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 451.947, 150480 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.10709, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 594.119, 215546 } kg +compflowStatistics, caprock: Dissolved component mass: { { 597.226, 0 }, { 351.809, 215187 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.21173 +compflowStatistics: Max component CFL number: 0.545261 +Time: 4.22e+08s, dt:1e+06s, Cycle: 1316 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.51e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.55e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.55e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.18e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00447271 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0651586 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75704e+07, 1.76096e+07, 1.76462e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.07118e+06, 5.14702e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.449 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.84098, 726.608 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2543.79, 704238 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.102, 212986 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1986.69, 491252 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.995, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2395.79, 704238 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2543.79, 0 }, { 1235.57, 702978 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75518e+07, 1.75641e+07, 1.75891e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05254e+06, 5.08992e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.778 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.37545, 222.402 } rm^3 +compflowStatistics, caprock: Phase mass: { 598.826, 215542 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.397, 65066.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 453.429, 150476 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.07172, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 595.754, 215542 } kg +compflowStatistics, caprock: Dissolved component mass: { { 598.826, 0 }, { 352.552, 215183 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.28303 +compflowStatistics: Max component CFL number: 0.541789 +Time: 4.23e+08s, dt:1e+06s, Cycle: 1317 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.57e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.57e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.33e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.13e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.13e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00445981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0622864 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75696e+07, 1.76088e+07, 1.76455e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0704e+06, 5.14624e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.448 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.83497, 726.613 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2541.03, 704243 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 557.003, 212986 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1984.03, 491257 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.861, 0.00107204 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2393.17, 704243 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2541.03, 0 }, { 1235.98, 702983 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7551e+07, 1.75634e+07, 1.75884e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05176e+06, 5.08914e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.778 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.3792, 222.398 } rm^3 +compflowStatistics, caprock: Phase mass: { 600.424, 215539 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.516, 65066.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 454.909, 150472 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.01393, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 597.411, 215539 } kg +compflowStatistics, caprock: Dissolved component mass: { { 600.424, 0 }, { 353.293, 215178 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.34562 +compflowStatistics: Max component CFL number: 0.57323 +Time: 4.24e+08s, dt:1e+06s, Cycle: 1318 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.80e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.80e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-05 ) ; + Last LinSolve(iter,res) = ( 7, 9.97e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00443593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627129 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75689e+07, 1.7608e+07, 1.76447e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06962e+06, 5.14546e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.448 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.82899, 726.619 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2538.28, 704248 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.909, 212985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1981.37, 491263 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.732, 0.00107203 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2390.55, 704248 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2538.28, 0 }, { 1236.4, 702987 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75502e+07, 1.75626e+07, 1.75876e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05098e+06, 5.08836e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.38295, 222.394 } rm^3 +compflowStatistics, caprock: Phase mass: { 602.023, 215535 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.639, 65066.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 456.384, 150468 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.08736, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 598.936, 215535 } kg +compflowStatistics, caprock: Dissolved component mass: { { 602.023, 0 }, { 354.029, 215174 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.31909 +compflowStatistics: Max component CFL number: 0.578972 +Time: 4.25e+08s, dt:1e+06s, Cycle: 1319 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.95e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.95e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.90e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 7.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.94e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.94e-05 ) ; + Last LinSolve(iter,res) = ( 7, 4.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440813 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632135 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75681e+07, 1.76073e+07, 1.76439e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06885e+06, 5.14469e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.447 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.82301, 726.624 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2535.54, 704253 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.815, 212985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1978.73, 491268 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.568, 0.00107203 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2387.97, 704253 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2535.54, 0 }, { 1236.81, 702992 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75494e+07, 1.75618e+07, 1.75868e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.05021e+06, 5.08759e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.38669, 222.391 } rm^3 +compflowStatistics, caprock: Phase mass: { 603.621, 215531 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.767, 65066.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 457.855, 150465 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.20332, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 600.418, 215531 } kg +compflowStatistics, caprock: Dissolved component mass: { { 603.621, 0 }, { 354.763, 215169 } } kg +compflowStatistics: Max phase CFL number: 2.31769 +compflowStatistics: Max component CFL number: 0.592405 +Time: 4.26e+08s, dt:1e+06s, Cycle: 1320 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.05e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.05e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.16e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.16e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.35e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00441195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682212 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.75673e+07, 1.76065e+07, 1.76432e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06809e+06, 5.14393e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.446 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.81705, 726.629 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2532.8, 704258 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.72, 212985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1976.08, 491273 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.446, 0.00107203 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2385.36, 704258 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2532.8, 0 }, { 1237.22, 702996 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75487e+07, 1.75611e+07, 1.75861e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04944e+06, 5.08682e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.39043, 222.387 } rm^3 +compflowStatistics, caprock: Phase mass: { 605.216, 215527 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 145.894, 65066.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 459.322, 150461 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.16133, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 602.054, 215527 } kg +compflowStatistics, caprock: Dissolved component mass: { { 605.216, 0 }, { 355.498, 215165 } } kg +compflowStatistics: Max phase CFL number: 2.32232 +compflowStatistics: Max component CFL number: 0.608094 +Time: 4.27e+08s, dt:1e+06s, Cycle: 1321 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.74e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.74e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00441223 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0937428 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75665e+07, 1.76057e+07, 1.76424e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06732e+06, 5.14316e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.446 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.81108, 726.635 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2530.07, 704263 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.625, 212985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1973.44, 491278 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.329, 0.00107202 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2382.74, 704263 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2530.07, 0 }, { 1237.62, 703001 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75479e+07, 1.75603e+07, 1.75853e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04867e+06, 5.08605e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.39417, 222.383 } rm^3 +compflowStatistics, caprock: Phase mass: { 606.806, 215524 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.021, 65066.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 460.785, 150457 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.21394, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 603.592, 215524 } kg +compflowStatistics, caprock: Dissolved component mass: { { 606.806, 0 }, { 356.234, 215160 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.33704 +compflowStatistics: Max component CFL number: 0.629149 +Time: 4.28e+08s, dt:1e+06s, Cycle: 1322 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.42e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.42e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.49e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440568 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.102887 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75658e+07, 1.7605e+07, 1.76416e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06655e+06, 5.14239e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.445 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.80513, 726.64 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2527.33, 704268 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.532, 212984 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1970.8, 491283 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.242, 0.00107202 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2380.09, 704268 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2527.33, 0 }, { 1238.03, 703005 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75471e+07, 1.75595e+07, 1.75845e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0479e+06, 5.08529e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.39789, 222.379 } rm^3 +compflowStatistics, caprock: Phase mass: { 608.393, 215520 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.148, 65066.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 462.245, 150454 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.26558, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 605.128, 215520 } kg +compflowStatistics, caprock: Dissolved component mass: { { 608.393, 0 }, { 356.973, 215156 } } kg +compflowStatistics: Max phase CFL number: 2.35828 +compflowStatistics: Max component CFL number: 0.653271 +Time: 4.29e+08s, dt:1e+06s, Cycle: 1323 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.98e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.03e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.03e-05 ) ; + Last LinSolve(iter,res) = ( 6, 8.36e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00441287 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0825537 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7565e+07, 1.76042e+07, 1.76408e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06578e+06, 5.14162e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.445 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.79918, 726.646 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2524.6, 704273 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.433, 212984 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1968.17, 491289 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 147.126, 0.00107202 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2377.48, 704273 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2524.6, 0 }, { 1238.44, 703010 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75464e+07, 1.75588e+07, 1.75837e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04713e+06, 5.08452e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.777 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.40161, 222.375 } rm^3 +compflowStatistics, caprock: Phase mass: { 609.976, 215516 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.274, 65066.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 463.702, 150450 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.19838, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 606.778, 215516 } kg +compflowStatistics, caprock: Dissolved component mass: { { 609.976, 0 }, { 357.713, 215151 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.38129 +compflowStatistics: Max component CFL number: 0.67647 +Time: 4.3e+08s, dt:1e+06s, Cycle: 1324 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.41e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.41e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00441093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694283 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75642e+07, 1.76034e+07, 1.76401e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06501e+06, 5.14085e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.444 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.79323, 726.651 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2521.87, 704277 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.333, 212984 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1965.54, 491294 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.985, 0.00107202 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2374.89, 704277 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2521.87, 0 }, { 1238.85, 703014 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75456e+07, 1.7558e+07, 1.7583e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04636e+06, 5.08374e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.776 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.40531, 222.371 } rm^3 +compflowStatistics, caprock: Phase mass: { 611.555, 215512 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.4, 65066.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 465.155, 150446 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.22692, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 608.328, 215512 } kg +compflowStatistics, caprock: Dissolved component mass: { { 611.555, 0 }, { 358.455, 215147 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.34896 +compflowStatistics: Max component CFL number: 0.669274 +Time: 4.31e+08s, dt:1e+06s, Cycle: 1325 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.78e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00440328 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691554 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75635e+07, 1.76026e+07, 1.76393e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06423e+06, 5.14007e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.444 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.78729, 726.656 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2519.15, 704282 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.23, 212983 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1962.92, 491299 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.868, 0.001072 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2372.28, 704282 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2519.15, 0 }, { 1239.25, 703019 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75448e+07, 1.75572e+07, 1.75822e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04559e+06, 5.08297e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.776 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.40901, 222.367 } rm^3 +compflowStatistics, caprock: Phase mass: { 613.131, 215509 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.523, 65066.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 466.608, 150442 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.06094, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 610.07, 215509 } kg +compflowStatistics, caprock: Dissolved component mass: { { 613.131, 0 }, { 359.198, 215142 } } kg +compflowStatistics: Max phase CFL number: 2.33426 +compflowStatistics: Max component CFL number: 0.658761 +Time: 4.32e+08s, dt:1e+06s, Cycle: 1326 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.50e-03 ) ; + Last LinSolve(iter,res) = ( 7, 8.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.28e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.28e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.25e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0043983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0825272 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75627e+07, 1.76019e+07, 1.76385e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06346e+06, 5.1393e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.443 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.78137, 726.662 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2516.43, 704287 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.12, 212983 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1960.31, 491304 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.633, 0.001072 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2369.8, 704287 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2516.43, 0 }, { 1239.66, 703023 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.7544e+07, 1.75564e+07, 1.75814e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04482e+06, 5.0822e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.776 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.4127, 222.363 } rm^3 +compflowStatistics, caprock: Phase mass: { 614.704, 215505 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.644, 65066.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 468.059, 150439 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.0214, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 611.682, 215505 } kg +compflowStatistics, caprock: Dissolved component mass: { { 614.704, 0 }, { 359.942, 215138 } } kg +compflowStatistics: Max phase CFL number: 2.32837 +compflowStatistics: Max component CFL number: 0.653095 +Time: 4.33e+08s, dt:1e+06s, Cycle: 1327 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.07e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.47e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439522 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0913061 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75619e+07, 1.76011e+07, 1.76378e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06269e+06, 5.13853e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.443 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.77545, 726.667 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2513.72, 704292 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 556.01, 212983 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1957.71, 491309 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.505, 0.00107199 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2367.21, 704292 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2513.72, 0 }, { 1240.06, 703028 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75433e+07, 1.75557e+07, 1.75807e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04405e+06, 5.08143e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.776 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.41639, 222.359 } rm^3 +compflowStatistics, caprock: Phase mass: { 616.273, 215501 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.767, 65066.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 469.506, 150435 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.06741, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 613.206, 215501 } kg +compflowStatistics, caprock: Dissolved component mass: { { 616.273, 0 }, { 360.687, 215133 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.33308 +compflowStatistics: Max component CFL number: 0.657195 +Time: 4.34e+08s, dt:1e+06s, Cycle: 1328 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.97e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.74e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439366 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0941458 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75612e+07, 1.76003e+07, 1.7637e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06192e+06, 5.13776e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.442 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.76954, 726.672 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2511.01, 704297 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.902, 212983 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1955.1, 491314 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.371, 0.00107198 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2364.63, 704297 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2511.01, 0 }, { 1240.45, 703032 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75425e+07, 1.75549e+07, 1.75799e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04328e+06, 5.08066e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.776 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.42007, 222.356 } rm^3 +compflowStatistics, caprock: Phase mass: { 617.839, 215498 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 146.89, 65066.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 470.949, 150431 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.07704, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 614.762, 215498 } kg +compflowStatistics, caprock: Dissolved component mass: { { 617.839, 0 }, { 361.434, 215129 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.34536 +compflowStatistics: Max component CFL number: 0.670572 +Time: 4.35e+08s, dt:1e+06s, Cycle: 1329 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.21e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00440484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.087838 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.75604e+07, 1.75996e+07, 1.76362e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06115e+06, 5.13699e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.441 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.76364, 726.678 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2508.3, 704302 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.788, 212982 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1952.51, 491319 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 146.178, 0.00107198 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2362.12, 704302 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2508.3, 0 }, { 1240.85, 703036 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75417e+07, 1.75541e+07, 1.75791e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04251e+06, 5.07989e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.776 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.42374, 222.352 } rm^3 +compflowStatistics, caprock: Phase mass: { 619.401, 215494 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.013, 65066.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 472.388, 150428 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.1382, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 616.263, 215494 } kg +compflowStatistics, caprock: Dissolved component mass: { { 619.401, 0 }, { 362.182, 215125 } } kg +compflowStatistics: Max phase CFL number: 2.35096 +compflowStatistics: Max component CFL number: 0.686222 +Time: 4.36e+08s, dt:1e+06s, Cycle: 1330 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.82e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.82e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00439683 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0710923 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75596e+07, 1.75988e+07, 1.76355e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.06038e+06, 5.13622e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.441 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.75774, 726.683 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2505.59, 704307 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.674, 212982 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1949.92, 491325 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.951, 0.00107197 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2359.64, 704307 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2505.59, 0 }, { 1241.25, 703041 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7541e+07, 1.75534e+07, 1.75784e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04174e+06, 5.07912e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.775 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.4274, 222.348 } rm^3 +compflowStatistics, caprock: Phase mass: { 620.96, 215490 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.138, 65066 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 473.822, 150424 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.16694, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 617.793, 215490 } kg +compflowStatistics, caprock: Dissolved component mass: { { 620.96, 0 }, { 362.931, 215120 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.30701 +compflowStatistics: Max component CFL number: 0.688666 +Time: 4.37e+08s, dt:1e+06s, Cycle: 1331 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.77e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00438409 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662942 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75588e+07, 1.7598e+07, 1.76347e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05961e+06, 5.13545e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.44 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.75186, 726.688 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2502.89, 704311 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.559, 212982 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1947.34, 491330 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.817, 0.00107197 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2357.08, 704311 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2502.89, 0 }, { 1241.64, 703045 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75402e+07, 1.75526e+07, 1.75776e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.04097e+06, 5.07835e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.775 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.43106, 222.344 } rm^3 +compflowStatistics, caprock: Phase mass: { 622.517, 215487 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.265, 65066 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 475.252, 150421 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.23318, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 619.283, 215487 } kg +compflowStatistics, caprock: Dissolved component mass: { { 622.517, 0 }, { 363.679, 215116 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.28128 +compflowStatistics: Max component CFL number: 0.706135 +Time: 4.38e+08s, dt:1e+06s, Cycle: 1332 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.47e-04 ) ; + Last LinSolve(iter,res) = ( 7, 8.28e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00436651 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0717208 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75581e+07, 1.75973e+07, 1.76339e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05885e+06, 5.13469e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.44 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.746, 726.694 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2500.21, 704316 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.448, 212981 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1944.76, 491335 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.693, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2354.51, 704316 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2500.21, 0 }, { 1242.03, 703050 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75394e+07, 1.75518e+07, 1.75768e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0402e+06, 5.07758e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.775 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.43471, 222.34 } rm^3 +compflowStatistics, caprock: Phase mass: { 624.071, 215483 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.392, 65066 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 476.679, 150417 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.24175, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 620.829, 215483 } kg +compflowStatistics, caprock: Dissolved component mass: { { 624.071, 0 }, { 364.428, 215111 } } kg +compflowStatistics: Max phase CFL number: 2.23663 +compflowStatistics: Max component CFL number: 0.722631 +Time: 4.39e+08s, dt:1e+06s, Cycle: 1333 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00434955 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0741723 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75573e+07, 1.75965e+07, 1.76332e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05808e+06, 5.13392e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.439 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.74015, 726.699 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2497.52, 704321 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.336, 212981 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1942.19, 491340 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.598, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2351.92, 704321 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2497.52, 0 }, { 1242.41, 703054 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75387e+07, 1.75511e+07, 1.75761e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03944e+06, 5.07682e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.775 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.43836, 222.337 } rm^3 +compflowStatistics, caprock: Phase mass: { 625.624, 215479 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.523, 65065.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 478.101, 150413 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.33663, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 622.287, 215479 } kg +compflowStatistics, caprock: Dissolved component mass: { { 625.624, 0 }, { 365.174, 215107 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.16158 +compflowStatistics: Max component CFL number: 0.732317 +Time: 4.4e+08s, dt:1e+06s, Cycle: 1334 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.87e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.46e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.46e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.73e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-05 ) ; + Last LinSolve(iter,res) = ( 7, 7.17e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0043335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0731951 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75566e+07, 1.75957e+07, 1.76324e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05732e+06, 5.13316e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.439 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.73431, 726.704 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2494.85, 704326 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.227, 212981 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1939.62, 491345 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.514, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2349.33, 704326 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2494.85, 0 }, { 1242.79, 703059 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75379e+07, 1.75503e+07, 1.75753e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03868e+06, 5.07606e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.775 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.44201, 222.333 } rm^3 +compflowStatistics, caprock: Phase mass: { 627.175, 215476 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.656, 65065.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 479.519, 150410 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.3818, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 623.793, 215476 } kg +compflowStatistics, caprock: Dissolved component mass: { { 627.175, 0 }, { 365.92, 215102 } } kg +compflowStatistics: Max phase CFL number: 2.03983 +compflowStatistics: Max component CFL number: 0.73075 +Time: 4.41e+08s, dt:1e+06s, Cycle: 1335 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.27e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.27e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.46e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00433231 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683299 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75558e+07, 1.7595e+07, 1.76316e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05657e+06, 5.13241e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.438 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.72847, 726.71 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2492.17, 704331 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.119, 212981 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1937.05, 491350 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.458, 0.00107197 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2346.71, 704331 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2492.17, 0 }, { 1243.17, 703063 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75372e+07, 1.75495e+07, 1.75745e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03792e+06, 5.0753e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.775 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.44564, 222.329 } rm^3 +compflowStatistics, caprock: Phase mass: { 628.723, 215472 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.792, 65065.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 480.932, 150406 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.44278, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 625.281, 215472 } kg +compflowStatistics, caprock: Dissolved component mass: { { 628.723, 0 }, { 366.664, 215098 } } kg +compflowStatistics: Max phase CFL number: 1.8505 +compflowStatistics: Max component CFL number: 0.711437 +Time: 4.42e+08s, dt:1e+06s, Cycle: 1336 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 +well_1Control: well is shut + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.37e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.37e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.56e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00433405 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599228 +coupledFlowAndWells: Time-step required will be increased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.75551e+07, 1.75942e+07, 1.76309e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05581e+06, 5.13165e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.438 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.72265, 726.715 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2489.5, 704335 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 555.013, 212980 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1934.49, 491355 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.285, 0.00107198 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2344.22, 704335 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2489.5, 0 }, { 1243.55, 703067 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75364e+07, 1.75488e+07, 1.75738e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03716e+06, 5.07455e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.774 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.44928, 222.325 } rm^3 +compflowStatistics, caprock: Phase mass: { 630.268, 215468 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 147.929, 65065.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 482.34, 150402 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.56184, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 626.706, 215468 } kg +compflowStatistics, caprock: Dissolved component mass: { { 630.268, 0 }, { 367.411, 215094 } } kg +compflowStatistics: Max phase CFL number: 1.57422 +compflowStatistics: Max component CFL number: 0.668211 +Time: 4.43e+08s, dt:1e+06s, Cycle: 1337 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.00e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.72e-07 ) ; + Last LinSolve(iter,res) = ( 8, 1.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00432918 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0590465 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75543e+07, 1.75935e+07, 1.76301e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05505e+06, 5.13089e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.437 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.71684, 726.72 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2486.84, 704340 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.905, 212980 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1931.93, 491360 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.155, 0.00107197 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2341.68, 704340 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2486.84, 0 }, { 1243.93, 703072 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75357e+07, 1.7548e+07, 1.7573e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03641e+06, 5.07379e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.774 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.4529, 222.321 } rm^3 +compflowStatistics, caprock: Phase mass: { 631.81, 215465 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.068, 65065.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 483.742, 150399 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.64282, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 628.167, 215465 } kg +compflowStatistics, caprock: Dissolved component mass: { { 631.81, 0 }, { 368.158, 215089 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.21413 +compflowStatistics: Max component CFL number: 0.59632 +Time: 4.44e+08s, dt:1e+06s, Cycle: 1338 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.14e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00430915 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629557 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75535e+07, 1.75927e+07, 1.76294e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0543e+06, 5.13014e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.436 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.71104, 726.725 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2484.18, 704345 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.803, 212980 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1929.38, 491365 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 145.032, 0.00107198 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2339.15, 704345 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2484.18, 0 }, { 1244.3, 703076 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75349e+07, 1.75473e+07, 1.75723e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03565e+06, 5.07304e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.774 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.45652, 222.318 } rm^3 +compflowStatistics, caprock: Phase mass: { 633.35, 215461 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.21, 65065.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 485.14, 150395 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.74194, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 629.608, 215461 } kg +compflowStatistics, caprock: Dissolved component mass: { { 633.35, 0 }, { 368.904, 215085 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 0.827315 +compflowStatistics: Max component CFL number: 0.556164 +Time: 4.45e+08s, dt:1e+06s, Cycle: 1339 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.85e-04 ) ; + Last LinSolve(iter,res) = ( 7, 7.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0042842 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657826 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75528e+07, 1.7592e+07, 1.76286e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05355e+06, 5.12939e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.436 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.70526, 726.731 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2481.54, 704350 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.703, 212980 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1926.83, 491370 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.964, 0.00107197 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2336.57, 704350 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2481.54, 0 }, { 1244.66, 703081 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75342e+07, 1.75465e+07, 1.75715e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0349e+06, 5.07229e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.774 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.46014, 222.314 } rm^3 +compflowStatistics, caprock: Phase mass: { 634.889, 215457 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.356, 65065.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 486.533, 150392 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.84255, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 631.046, 215457 } kg +compflowStatistics, caprock: Dissolved component mass: { { 634.889, 0 }, { 369.647, 215080 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 0.851006 +compflowStatistics: Max component CFL number: 0.561604 +Time: 4.46e+08s, dt:1e+06s, Cycle: 1340 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.75e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.67e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00426792 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0663851 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75521e+07, 1.75912e+07, 1.76279e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0528e+06, 5.12864e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.435 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.69949, 726.736 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2478.89, 704355 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.606, 212979 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1924.29, 491375 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.897, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2334, 704355 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2478.89, 0 }, { 1245.03, 703085 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75334e+07, 1.75458e+07, 1.75708e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03416e+06, 5.07154e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.774 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.46376, 222.31 } rm^3 +compflowStatistics, caprock: Phase mass: { 636.428, 215454 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.506, 65065.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 487.922, 150388 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 3.89801, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 632.53, 215454 } kg +compflowStatistics, caprock: Dissolved component mass: { { 636.428, 0 }, { 370.385, 215076 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.00753 +compflowStatistics: Max component CFL number: 0.565111 +Time: 4.47e+08s, dt:1e+06s, Cycle: 1341 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.69e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.66e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00424871 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643501 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75513e+07, 1.75905e+07, 1.76272e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05206e+06, 5.1279e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.435 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.69373, 726.741 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2476.26, 704359 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.512, 212979 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1921.74, 491380 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.823, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2331.43, 704359 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2476.26, 0 }, { 1245.39, 703089 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75327e+07, 1.75451e+07, 1.75701e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03341e+06, 5.0708e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.774 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.46738, 222.306 } rm^3 +compflowStatistics, caprock: Phase mass: { 637.968, 215450 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.662, 65065.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 489.306, 150384 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.04759, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 633.92, 215450 } kg +compflowStatistics, caprock: Dissolved component mass: { { 637.968, 0 }, { 371.117, 215072 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.12362 +compflowStatistics: Max component CFL number: 0.568502 +Time: 4.48e+08s, dt:1e+06s, Cycle: 1342 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.11e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.11e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.62e-07 ) ; + Last LinSolve(iter,res) = ( 8, 9.46e-04 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00422096 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675392 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75506e+07, 1.75898e+07, 1.76264e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05132e+06, 5.12716e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.434 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.68799, 726.746 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2473.63, 704364 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.421, 212979 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1919.21, 491385 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.709, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2328.92, 704364 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2473.63, 0 }, { 1245.75, 703094 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75319e+07, 1.75443e+07, 1.75693e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03267e+06, 5.07006e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.773 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.47099, 222.302 } rm^3 +compflowStatistics, caprock: Phase mass: { 639.506, 215447 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.82, 65065.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 490.686, 150381 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.0544, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 635.452, 215447 } kg +compflowStatistics, caprock: Dissolved component mass: { { 639.506, 0 }, { 371.849, 215067 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.15169 +compflowStatistics: Max component CFL number: 0.587396 +Time: 4.49e+08s, dt:1e+06s, Cycle: 1343 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.19e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.19e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00421027 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0710138 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75499e+07, 1.7589e+07, 1.76257e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.05059e+06, 5.12643e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.434 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.68226, 726.751 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2471.01, 704369 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.328, 212978 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1916.68, 491390 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.617, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2326.39, 704369 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2471.01, 0 }, { 1246.1, 703098 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75312e+07, 1.75436e+07, 1.75686e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03194e+06, 5.06933e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.773 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.4746, 222.299 } rm^3 +compflowStatistics, caprock: Phase mass: { 641.041, 215443 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 148.979, 65065.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 492.063, 150377 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.11137, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 636.93, 215443 } kg +compflowStatistics, caprock: Dissolved component mass: { { 641.041, 0 }, { 372.58, 215063 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.18469 +compflowStatistics: Max component CFL number: 0.605661 +Time: 4.5e+08s, dt:1e+06s, Cycle: 1344 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.20e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00419695 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679673 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75491e+07, 1.75883e+07, 1.7625e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04985e+06, 5.1257e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.433 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.67655, 726.757 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2468.39, 704373 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.238, 212978 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1914.15, 491395 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.559, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2323.83, 704373 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2468.39, 0 }, { 1246.45, 703102 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75305e+07, 1.75429e+07, 1.75679e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03121e+06, 5.06859e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.773 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.47821, 222.295 } rm^3 +compflowStatistics, caprock: Phase mass: { 642.574, 215439 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 149.138, 65065.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 493.435, 150374 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.23835, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 638.335, 215439 } kg +compflowStatistics, caprock: Dissolved component mass: { { 642.574, 0 }, { 373.312, 215059 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.21498 +compflowStatistics: Max component CFL number: 0.621512 +Time: 4.51e+08s, dt:1e+06s, Cycle: 1345 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.27e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.27e-05 ) ; + Last LinSolve(iter,res) = ( 7, 5.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00419066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691362 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75484e+07, 1.75876e+07, 1.76242e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04912e+06, 5.12497e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.433 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.67084, 726.762 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2465.78, 704378 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.149, 212978 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1911.63, 491400 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.48, 0.00107196 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2321.3, 704378 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2465.78, 0 }, { 1246.8, 703107 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75297e+07, 1.75421e+07, 1.75671e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.03048e+06, 5.06787e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.773 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.4818, 222.291 } rm^3 +compflowStatistics, caprock: Phase mass: { 644.103, 215436 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 149.298, 65065.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 494.805, 150370 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.14209, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 639.961, 215436 } kg +compflowStatistics, caprock: Dissolved component mass: { { 644.103, 0 }, { 374.044, 215054 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.23937 +compflowStatistics: Max component CFL number: 0.635767 +Time: 4.52e+08s, dt:1e+06s, Cycle: 1346 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 7, 6.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.30e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.30e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.49e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00418453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0681545 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75477e+07, 1.75869e+07, 1.76235e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0484e+06, 5.12424e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.432 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.66514, 726.767 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2463.17, 704383 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 554.062, 212978 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1909.11, 491405 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.441, 0.00107195 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2318.73, 704383 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2463.17, 0 }, { 1247.15, 703111 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7529e+07, 1.75414e+07, 1.75664e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02975e+06, 5.06714e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.773 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.48539, 222.287 } rm^3 +compflowStatistics, caprock: Phase mass: { 645.63, 215432 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 149.458, 65065.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 496.172, 150366 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.22653, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 641.403, 215432 } kg +compflowStatistics, caprock: Dissolved component mass: { { 645.63, 0 }, { 374.776, 215050 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.2578 +compflowStatistics: Max component CFL number: 0.649692 +Time: 4.53e+08s, dt:1e+06s, Cycle: 1347 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.55e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.55e-04 ) ; + Last LinSolve(iter,res) = ( 7, 6.83e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00416383 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0760312 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.75469e+07, 1.75861e+07, 1.76228e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04767e+06, 5.12351e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.432 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.65945, 726.772 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2460.57, 704388 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.978, 212977 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1906.59, 491410 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.415, 0.00107195 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2316.15, 704388 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2460.57, 0 }, { 1247.5, 703115 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75283e+07, 1.75407e+07, 1.75657e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02902e+06, 5.06641e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.773 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.48898, 222.284 } rm^3 +compflowStatistics, caprock: Phase mass: { 647.154, 215429 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 149.621, 65065.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 497.533, 150363 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.36242, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 642.792, 215429 } kg +compflowStatistics, caprock: Dissolved component mass: { { 647.154, 0 }, { 375.507, 215046 } } kg +compflowStatistics: Max phase CFL number: 1.26263 +compflowStatistics: Max component CFL number: 0.664815 +Time: 4.54e+08s, dt:1e+06s, Cycle: 1348 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.50e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.59e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.59e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.02e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00415123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0750304 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75462e+07, 1.75854e+07, 1.76221e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04694e+06, 5.12278e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.431 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.65377, 726.777 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2457.97, 704392 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.897, 212977 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1904.07, 491415 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.357, 0.00107194 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2313.62, 704392 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2457.97, 0 }, { 1247.85, 703120 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75276e+07, 1.75399e+07, 1.7565e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02829e+06, 5.06568e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.49256, 222.28 } rm^3 +compflowStatistics, caprock: Phase mass: { 648.676, 215425 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 149.786, 65065.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 498.889, 150359 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.48365, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 644.192, 215425 } kg +compflowStatistics, caprock: Dissolved component mass: { { 648.676, 0 }, { 376.238, 215041 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.25739 +compflowStatistics: Max component CFL number: 0.678922 +Time: 4.55e+08s, dt:1e+06s, Cycle: 1349 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.90e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.64e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0041402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730023 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75455e+07, 1.75847e+07, 1.76213e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04622e+06, 5.12206e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.431 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.64811, 726.782 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2455.38, 704397 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.816, 212977 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1901.56, 491420 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.283, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2311.1, 704397 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2455.38, 0 }, { 1248.19, 703124 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75268e+07, 1.75392e+07, 1.75642e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02757e+06, 5.06496e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.49613, 222.276 } rm^3 +compflowStatistics, caprock: Phase mass: { 650.195, 215421 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 149.953, 65065.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 500.242, 150356 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.51968, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 645.675, 215421 } kg +compflowStatistics, caprock: Dissolved component mass: { { 650.195, 0 }, { 376.969, 215037 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.25667 +compflowStatistics: Max component CFL number: 0.687394 +Time: 4.56e+08s, dt:1e+06s, Cycle: 1350 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.45e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.45e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.19e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0041315 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730996 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75448e+07, 1.7584e+07, 1.76206e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04549e+06, 5.12134e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.43 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.64245, 726.788 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2452.79, 704402 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.733, 212977 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1899.06, 491425 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.131, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2308.66, 704402 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2452.79, 0 }, { 1248.53, 703128 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75261e+07, 1.75385e+07, 1.75635e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02685e+06, 5.06424e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.4997, 222.272 } rm^3 +compflowStatistics, caprock: Phase mass: { 651.712, 215418 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 150.122, 65065.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 501.59, 150352 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.66719, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 647.045, 215418 } kg +compflowStatistics, caprock: Dissolved component mass: { { 651.712, 0 }, { 377.698, 215033 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.25169 +compflowStatistics: Max component CFL number: 0.691191 +Time: 4.57e+08s, dt:1e+06s, Cycle: 1351 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.90e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.90e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.48e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00413219 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716538 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75441e+07, 1.75832e+07, 1.76199e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04477e+06, 5.12062e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.43 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.6368, 726.793 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2450.21, 704406 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.65, 212976 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1896.56, 491430 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.137, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2306.07, 704406 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2450.21, 0 }, { 1248.87, 703133 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75254e+07, 1.75378e+07, 1.75628e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02613e+06, 5.06352e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.50327, 222.269 } rm^3 +compflowStatistics, caprock: Phase mass: { 653.227, 215414 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 150.295, 65065.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 502.932, 150349 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.79979, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 648.427, 215414 } kg +compflowStatistics, caprock: Dissolved component mass: { { 653.227, 0 }, { 378.426, 215028 } } kg +compflowStatistics: Max phase CFL number: 1.23883 +compflowStatistics: Max component CFL number: 0.691528 +Time: 4.58e+08s, dt:1e+06s, Cycle: 1352 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.53e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.53e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.63e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.004123 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728675 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75433e+07, 1.75825e+07, 1.76192e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04405e+06, 5.1199e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.429 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.63116, 726.798 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2447.63, 704411 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.566, 212976 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1894.07, 491435 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.113, 0.00107192 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2303.52, 704411 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2447.63, 0 }, { 1249.21, 703137 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75247e+07, 1.75371e+07, 1.75621e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02541e+06, 5.0628e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.50683, 222.265 } rm^3 +compflowStatistics, caprock: Phase mass: { 654.74, 215411 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 150.468, 65065.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 504.273, 150345 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.81145, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 649.929, 215411 } kg +compflowStatistics, caprock: Dissolved component mass: { { 654.74, 0 }, { 379.152, 215024 } } kg +compflowStatistics: Max phase CFL number: 1.21401 +compflowStatistics: Max component CFL number: 0.687043 +Time: 4.59e+08s, dt:1e+06s, Cycle: 1353 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.66e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.33e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.0040998 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0743859 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75426e+07, 1.75818e+07, 1.76185e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04334e+06, 5.11918e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.428 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.62553, 726.803 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2445.06, 704416 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.478, 212976 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1891.58, 491440 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.958, 0.00107194 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2301.1, 704416 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2445.06, 0 }, { 1249.54, 703141 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7524e+07, 1.75364e+07, 1.75614e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02469e+06, 5.06208e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.772 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.51039, 222.261 } rm^3 +compflowStatistics, caprock: Phase mass: { 656.254, 215407 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 150.642, 65065.5 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 505.612, 150342 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.73233, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 651.522, 215407 } kg +compflowStatistics, caprock: Dissolved component mass: { { 656.254, 0 }, { 379.873, 215020 } } kg +compflowStatistics: Max phase CFL number: 1.16352 +compflowStatistics: Max component CFL number: 0.680923 +Time: 4.6e+08s, dt:1e+06s, Cycle: 1354 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.73e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.48e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00408899 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689149 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75419e+07, 1.75811e+07, 1.76178e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04262e+06, 5.11847e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.428 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.61992, 726.808 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2442.5, 704420 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.39, 212976 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1889.11, 491445 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.982, 0.00107195 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2298.51, 704420 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2442.5, 0 }, { 1249.88, 703146 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75233e+07, 1.75356e+07, 1.75607e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02397e+06, 5.06137e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.51395, 222.257 } rm^3 +compflowStatistics, caprock: Phase mass: { 657.765, 215404 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 150.82, 65065.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 506.946, 150338 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 4.8822, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 652.883, 215404 } kg +compflowStatistics, caprock: Dissolved component mass: { { 657.765, 0 }, { 380.593, 215015 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.07447 +compflowStatistics: Max component CFL number: 0.67446 +Time: 4.61e+08s, dt:1e+06s, Cycle: 1355 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.04e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.08e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00407039 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0729361 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75412e+07, 1.75804e+07, 1.7617e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04191e+06, 5.11776e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.427 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.61432, 726.813 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2439.94, 704425 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.301, 212975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1886.63, 491449 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.015, 0.00107194 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2295.92, 704425 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2439.94, 0 }, { 1250.21, 703150 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75226e+07, 1.75349e+07, 1.75599e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02326e+06, 5.06066e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.5175, 222.254 } rm^3 +compflowStatistics, caprock: Phase mass: { 659.275, 215400 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 151, 65065.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 508.275, 150335 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.00956, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 654.266, 215400 } kg +compflowStatistics, caprock: Dissolved component mass: { { 659.275, 0 }, { 381.311, 215011 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 0.933565 +compflowStatistics: Max component CFL number: 0.667922 +Time: 4.62e+08s, dt:1e+06s, Cycle: 1356 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.40e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.87e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.09e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0040487 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0746494 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75405e+07, 1.75797e+07, 1.76163e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.04121e+06, 5.11705e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.427 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.60873, 726.818 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2437.38, 704429 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.215, 212975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1884.17, 491454 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.062, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2293.32, 704429 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2437.38, 0 }, { 1250.54, 703154 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75219e+07, 1.75342e+07, 1.75592e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02256e+06, 5.05995e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.52105, 222.25 } rm^3 +compflowStatistics, caprock: Phase mass: { 660.784, 215396 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 151.182, 65065.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 509.602, 150331 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.00938, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 655.775, 215396 } kg +compflowStatistics, caprock: Dissolved component mass: { { 660.784, 0 }, { 382.026, 215007 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 0.724401 +compflowStatistics: Max component CFL number: 0.662661 +Time: 4.63e+08s, dt:1e+06s, Cycle: 1357 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.00e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.00e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.59e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.68e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.68e-01 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.42e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.125: ( Rflow ) = ( 5.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Line search @ 0.062: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.33e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00402842 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0789134 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75398e+07, 1.7579e+07, 1.76156e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0405e+06, 5.11635e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.426 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.60316, 726.823 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2434.84, 704434 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.13, 212975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1881.71, 491459 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.037, 0.00107192 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2290.8, 704434 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2434.84, 0 }, { 1250.86, 703159 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75212e+07, 1.75335e+07, 1.75585e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02185e+06, 5.05925e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.5246, 222.246 } rm^3 +compflowStatistics, caprock: Phase mass: { 662.292, 215393 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 151.367, 65065.4 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 510.925, 150328 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.14624, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 657.146, 215393 } kg +compflowStatistics, caprock: Dissolved component mass: { { 662.292, 0 }, { 382.738, 215003 } } kg +compflowStatistics: Max phase CFL number: 0.707441 +compflowStatistics: Max component CFL number: 0.658915 +Time: 4.64e+08s, dt:1e+06s, Cycle: 1358 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.51e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.34e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00400962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728447 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75391e+07, 1.75783e+07, 1.76149e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0398e+06, 5.11565e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.426 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.59759, 726.828 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2432.3, 704439 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 553.045, 212975 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1879.25, 491464 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.091, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2288.2, 704439 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2432.3, 0 }, { 1251.19, 703163 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75205e+07, 1.75328e+07, 1.75578e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02115e+06, 5.05855e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.52815, 222.243 } rm^3 +compflowStatistics, caprock: Phase mass: { 663.8, 215389 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 151.556, 65065.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 512.244, 150324 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.22254, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 658.577, 215389 } kg +compflowStatistics, caprock: Dissolved component mass: { { 663.8, 0 }, { 383.446, 214998 } } kg +compflowStatistics: Max phase CFL number: 0.672454 +compflowStatistics: Max component CFL number: 0.655207 +Time: 4.65e+08s, dt:1e+06s, Cycle: 1359 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.81e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.81e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.21e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.18e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.68e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00398359 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0622146 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75384e+07, 1.75776e+07, 1.76143e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03911e+06, 5.11495e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.425 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.59203, 726.833 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2429.76, 704443 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.961, 212974 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1876.8, 491469 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.083, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2285.68, 704443 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2429.76, 0 }, { 1251.52, 703167 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75198e+07, 1.75321e+07, 1.75572e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.02045e+06, 5.05785e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.53169, 222.239 } rm^3 +compflowStatistics, caprock: Phase mass: { 665.306, 215386 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 151.749, 65065.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 513.557, 150320 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.34602, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 659.96, 215386 } kg +compflowStatistics, caprock: Dissolved component mass: { { 665.306, 0 }, { 384.151, 214994 } } kg +compflowStatistics: Max phase CFL number: 1.94676 +compflowStatistics: Max component CFL number: 0.666791 +Time: 4.66e+08s, dt:1e+06s, Cycle: 1360 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.45e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.52e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.52e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.51e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00397587 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0702225 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75377e+07, 1.75769e+07, 1.76136e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03841e+06, 5.11425e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.425 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.58649, 726.838 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2427.23, 704448 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.874, 212974 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1874.35, 491474 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.134, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2283.09, 704448 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2427.23, 0 }, { 1251.84, 703171 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75191e+07, 1.75314e+07, 1.75565e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01976e+06, 5.05715e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.771 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.53523, 222.235 } rm^3 +compflowStatistics, caprock: Phase mass: { 666.811, 215382 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 151.944, 65065.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 514.866, 150317 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.5262, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 661.284, 215382 } kg +compflowStatistics, caprock: Dissolved component mass: { { 666.811, 0 }, { 384.855, 214990 } } kg +compflowStatistics: Max phase CFL number: 3.08381 +compflowStatistics: Max component CFL number: 0.689743 +Time: 4.67e+08s, dt:1e+06s, Cycle: 1361 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.19e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.80e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00396321 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0707701 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.7537e+07, 1.75762e+07, 1.76129e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03772e+06, 5.11356e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.424 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.58095, 726.843 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2424.7, 704452 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.789, 212974 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1871.91, 491479 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.17, 0.00107194 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2280.53, 704452 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2424.7, 0 }, { 1252.16, 703176 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75184e+07, 1.75308e+07, 1.75558e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01906e+06, 5.05646e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.77 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.53877, 222.232 } rm^3 +compflowStatistics, caprock: Phase mass: { 668.314, 215379 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 152.144, 65065.3 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 516.17, 150313 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.66428, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 662.65, 215379 } kg +compflowStatistics, caprock: Dissolved component mass: { { 668.314, 0 }, { 385.555, 214985 } } kg +compflowStatistics: Max phase CFL number: 3.49684 +compflowStatistics: Max component CFL number: 0.703389 +Time: 4.68e+08s, dt:1e+06s, Cycle: 1362 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.61e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.56e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.56e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.44e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.0039373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629246 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75363e+07, 1.75755e+07, 1.76122e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03703e+06, 5.11287e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.424 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.57543, 726.848 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2422.18, 704457 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.708, 212974 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1869.48, 491483 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.181, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2278, 704457 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2422.18, 0 }, { 1252.48, 703180 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75177e+07, 1.75301e+07, 1.75551e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01837e+06, 5.05577e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.77 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.54231, 222.228 } rm^3 +compflowStatistics, caprock: Phase mass: { 669.817, 215375 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 152.348, 65065.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 517.469, 150310 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 5.84645, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 663.97, 215375 } kg +compflowStatistics, caprock: Dissolved component mass: { { 669.817, 0 }, { 386.253, 214981 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.61731 +compflowStatistics: Max component CFL number: 0.707346 +Time: 4.69e+08s, dt:1e+06s, Cycle: 1363 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.66e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.01e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.55e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00392855 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0598855 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75357e+07, 1.75748e+07, 1.76115e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03634e+06, 5.11219e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.423 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.56992, 726.853 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2419.67, 704462 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.624, 212973 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1867.05, 491488 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.182, 0.00107192 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2275.49, 704461 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2419.67, 0 }, { 1252.8, 703184 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7517e+07, 1.75294e+07, 1.75544e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01769e+06, 5.05509e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.77 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.54584, 222.224 } rm^3 +compflowStatistics, caprock: Phase mass: { 671.317, 215372 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 152.555, 65065.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 518.763, 150306 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.01724, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 665.3, 215372 } kg +compflowStatistics, caprock: Dissolved component mass: { { 671.317, 0 }, { 386.949, 214977 } } kg +compflowStatistics: Max phase CFL number: 3.70516 +compflowStatistics: Max component CFL number: 0.704662 +Time: 4.7e+08s, dt:1e+06s, Cycle: 1364 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.95e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.98e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00391981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0680694 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7535e+07, 1.75742e+07, 1.76108e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03566e+06, 5.1115e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.423 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.56442, 726.859 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2417.16, 704466 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.539, 212973 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1864.62, 491493 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.074, 0.00107193 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2273.09, 704466 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2417.16, 0 }, { 1253.11, 703188 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75163e+07, 1.75287e+07, 1.75537e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.017e+06, 5.0544e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.77 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.54937, 222.221 } rm^3 +compflowStatistics, caprock: Phase mass: { 672.817, 215368 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 152.764, 65065.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 520.053, 150303 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.18734, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 666.63, 215368 } kg +compflowStatistics, caprock: Dissolved component mass: { { 672.817, 0 }, { 387.642, 214973 } } kg +compflowStatistics: Max phase CFL number: 3.76877 +compflowStatistics: Max component CFL number: 0.700768 +Time: 4.71e+08s, dt:1e+06s, Cycle: 1365 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.12e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.60e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389523 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0794359 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75343e+07, 1.75735e+07, 1.76101e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03498e+06, 5.11082e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.422 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.55893, 726.863 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2414.66, 704471 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.455, 212973 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1862.2, 491498 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.056, 0.00107192 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2270.6, 704471 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2414.66, 0 }, { 1253.43, 703193 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75156e+07, 1.7528e+07, 1.7553e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01632e+06, 5.05372e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.77 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.5529, 222.217 } rm^3 +compflowStatistics, caprock: Phase mass: { 674.314, 215365 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 152.973, 65065.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 521.341, 150299 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.15145, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 668.163, 215365 } kg +compflowStatistics, caprock: Dissolved component mass: { { 674.314, 0 }, { 388.335, 214969 } } kg +compflowStatistics: Max phase CFL number: 3.80252 +compflowStatistics: Max component CFL number: 0.725425 +Time: 4.72e+08s, dt:1e+06s, Cycle: 1366 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.35e-06 ) ; + Last LinSolve(iter,res) = ( 7, 4.75e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00388351 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0824927 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75336e+07, 1.75728e+07, 1.76095e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0343e+06, 5.11014e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.422 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.55345, 726.868 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2412.16, 704475 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.374, 212973 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1859.79, 491503 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.059, 0.00107192 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2268.1, 704475 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2412.16, 0 }, { 1253.74, 703197 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7515e+07, 1.75273e+07, 1.75524e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01564e+06, 5.05304e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.77 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.55642, 222.213 } rm^3 +compflowStatistics, caprock: Phase mass: { 675.809, 215361 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 153.182, 65065.2 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 522.627, 150296 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.2402, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 669.569, 215361 } kg +compflowStatistics, caprock: Dissolved component mass: { { 675.809, 0 }, { 389.027, 214964 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.80281 +compflowStatistics: Max component CFL number: 0.742641 +Time: 4.73e+08s, dt:1e+06s, Cycle: 1367 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.88e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.55e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.55e-06 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00389338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.08128 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75329e+07, 1.75721e+07, 1.76088e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03362e+06, 5.10947e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.421 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.54798, 726.873 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2409.67, 704480 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.293, 212972 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1857.37, 491507 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 144.06, 0.00107191 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2265.61, 704480 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2409.67, 0 }, { 1254.05, 703201 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75143e+07, 1.75267e+07, 1.75517e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01497e+06, 5.05237e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.55993, 222.21 } rm^3 +compflowStatistics, caprock: Phase mass: { 677.301, 215358 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 153.393, 65065.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 523.908, 150292 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.33943, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 670.962, 215358 } kg +compflowStatistics, caprock: Dissolved component mass: { { 677.301, 0 }, { 389.719, 214960 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.74745 +compflowStatistics: Max component CFL number: 0.743616 +Time: 4.74e+08s, dt:1e+06s, Cycle: 1368 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.44e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.13e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.13e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.99e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00388746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065754 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75323e+07, 1.75715e+07, 1.76081e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03295e+06, 5.10879e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.421 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.54252, 726.878 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2407.18, 704484 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.208, 212972 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1854.97, 491512 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.952, 0.00107191 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2263.22, 704484 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2407.18, 0 }, { 1254.36, 703205 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75136e+07, 1.7526e+07, 1.7551e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01429e+06, 5.05169e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.56344, 222.206 } rm^3 +compflowStatistics, caprock: Phase mass: { 678.791, 215354 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 153.606, 65065.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 525.185, 150289 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.49141, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 672.3, 215354 } kg +compflowStatistics, caprock: Dissolved component mass: { { 678.791, 0 }, { 390.409, 214956 } } kg +compflowStatistics: Max phase CFL number: 3.64304 +compflowStatistics: Max component CFL number: 0.736719 +Time: 4.75e+08s, dt:1e+06s, Cycle: 1369 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.05e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.20e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.51e-06 ) ; + Last LinSolve(iter,res) = ( 7, 2.05e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00386888 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0579363 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75316e+07, 1.75708e+07, 1.76074e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03227e+06, 5.10811e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.42 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.53707, 726.883 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2404.69, 704489 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.124, 212972 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1852.57, 491517 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.895, 0.00107191 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2260.8, 704489 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2404.69, 0 }, { 1254.66, 703209 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75129e+07, 1.75253e+07, 1.75503e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01361e+06, 5.05101e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.56694, 222.202 } rm^3 +compflowStatistics, caprock: Phase mass: { 680.28, 215351 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 153.822, 65065.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 526.458, 150286 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.61142, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 673.668, 215351 } kg +compflowStatistics, caprock: Dissolved component mass: { { 680.28, 0 }, { 391.097, 214952 } } kg +compflowStatistics: Max phase CFL number: 3.46165 +compflowStatistics: Max component CFL number: 0.720915 +Time: 4.76e+08s, dt:1e+06s, Cycle: 1370 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.93e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.93e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.93e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00385084 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0571016 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75309e+07, 1.75701e+07, 1.76068e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0316e+06, 5.10744e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.42 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.53162, 726.888 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2402.21, 704493 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 552.039, 212972 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1850.17, 491522 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.866, 0.0010719 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2258.34, 704493 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2402.21, 0 }, { 1254.97, 703214 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75123e+07, 1.75246e+07, 1.75497e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01294e+06, 5.05034e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.57045, 222.199 } rm^3 +compflowStatistics, caprock: Phase mass: { 681.768, 215347 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 154.042, 65065.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 527.726, 150282 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.78682, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 674.981, 215347 } kg +compflowStatistics, caprock: Dissolved component mass: { { 681.768, 0 }, { 391.78, 214947 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.1372 +compflowStatistics: Max component CFL number: 0.688992 +Time: 4.77e+08s, dt:1e+06s, Cycle: 1371 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.12e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.12e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.24e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.66e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00383786 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667995 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75303e+07, 1.75694e+07, 1.76061e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03093e+06, 5.10677e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.419 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.52619, 726.893 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2399.74, 704498 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.954, 212971 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1847.78, 491526 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.759, 0.00107188 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2255.98, 704498 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2399.74, 0 }, { 1255.28, 703218 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75116e+07, 1.7524e+07, 1.7549e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01227e+06, 5.04967e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.57395, 222.195 } rm^3 +compflowStatistics, caprock: Phase mass: { 683.255, 215344 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 154.266, 65065.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 528.989, 150279 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 6.99268, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 676.262, 215344 } kg +compflowStatistics, caprock: Dissolved component mass: { { 683.255, 0 }, { 392.462, 214943 } } kg +compflowStatistics: Max phase CFL number: 2.54257 +compflowStatistics: Max component CFL number: 0.629653 +Time: 4.78e+08s, dt:1e+06s, Cycle: 1372 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.91e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.91e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.67e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.67e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.01e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00383135 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.071791 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75296e+07, 1.75688e+07, 1.76054e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.03026e+06, 5.1061e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.419 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.52077, 726.898 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2397.27, 704502 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.868, 212971 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1845.4, 491531 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.772, 0.00107187 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2253.49, 704502 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2397.27, 0 }, { 1255.58, 703222 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75109e+07, 1.75233e+07, 1.75483e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0116e+06, 5.049e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.57744, 222.191 } rm^3 +compflowStatistics, caprock: Phase mass: { 684.739, 215340 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 154.492, 65065 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 530.247, 150275 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.16782, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 677.572, 215340 } kg +compflowStatistics, caprock: Dissolved component mass: { { 684.739, 0 }, { 393.142, 214939 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.6215 +compflowStatistics: Max component CFL number: 0.625688 +Time: 4.79e+08s, dt:1e+06s, Cycle: 1373 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.31e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.63e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.91e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00382738 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.070916 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75289e+07, 1.75681e+07, 1.76048e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02959e+06, 5.10544e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.419 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.51535, 726.903 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2394.8, 704507 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.781, 212971 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1843.02, 491536 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.732, 0.00107186 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2251.07, 704507 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2394.8, 0 }, { 1255.89, 703226 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75103e+07, 1.75226e+07, 1.75477e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01094e+06, 5.04834e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.769 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.58094, 222.188 } rm^3 +compflowStatistics, caprock: Phase mass: { 686.222, 215337 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 154.721, 65065 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 531.5, 150272 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.36974, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 678.852, 215337 } kg +compflowStatistics, caprock: Dissolved component mass: { { 686.222, 0 }, { 393.822, 214935 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 0.86171 +compflowStatistics: Max component CFL number: 0.624066 +Time: 4.8e+08s, dt:1e+06s, Cycle: 1374 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.06e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.54e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00381851 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675837 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75283e+07, 1.75675e+07, 1.76041e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02893e+06, 5.10477e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.418 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.50995, 726.908 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2392.34, 704511 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.693, 212971 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1840.64, 491541 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.721, 0.00107185 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2248.61, 704511 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2392.34, 0 }, { 1256.19, 703230 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75096e+07, 1.7522e+07, 1.7547e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.01027e+06, 5.04767e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.58442, 222.184 } rm^3 +compflowStatistics, caprock: Phase mass: { 687.702, 215333 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 154.952, 65065 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 532.749, 150268 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.53895, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 680.163, 215333 } kg +compflowStatistics, caprock: Dissolved component mass: { { 687.702, 0 }, { 394.5, 214931 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 1.89561 +compflowStatistics: Max component CFL number: 0.623735 +Time: 4.81e+08s, dt:1e+06s, Cycle: 1375 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.80e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.33e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.33e-07 ) ; + Last LinSolve(iter,res) = ( 8, 2.59e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00380517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0622167 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75276e+07, 1.75668e+07, 1.76034e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02826e+06, 5.10411e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.418 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.50455, 726.913 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2389.88, 704516 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.605, 212970 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1838.27, 491545 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.694, 0.00107185 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2246.18, 704516 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2389.88, 0 }, { 1256.5, 703234 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75089e+07, 1.75213e+07, 1.75463e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00961e+06, 5.04701e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.5879, 222.18 } rm^3 +compflowStatistics, caprock: Phase mass: { 689.18, 215330 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 155.186, 65065 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 533.994, 150265 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.71351, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 681.466, 215330 } kg +compflowStatistics, caprock: Dissolved component mass: { { 689.18, 0 }, { 395.177, 214927 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.40592 +compflowStatistics: Max component CFL number: 0.623916 +Time: 4.82e+08s, dt:1e+06s, Cycle: 1376 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.68e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00379734 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0725079 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75269e+07, 1.75661e+07, 1.76028e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0276e+06, 5.10345e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.417 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.49916, 726.918 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2387.42, 704520 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.516, 212970 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1835.91, 491550 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.726, 0.00107185 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2243.7, 704520 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2387.42, 0 }, { 1256.8, 703239 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75083e+07, 1.75207e+07, 1.75457e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00894e+06, 5.04635e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.59138, 222.177 } rm^3 +compflowStatistics, caprock: Phase mass: { 690.656, 215326 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 155.423, 65065 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 535.233, 150261 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 7.887, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 682.769, 215326 } kg +compflowStatistics, caprock: Dissolved component mass: { { 690.656, 0 }, { 395.853, 214922 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.69041 +compflowStatistics: Max component CFL number: 0.625263 +Time: 4.83e+08s, dt:1e+06s, Cycle: 1377 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.84e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.84e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00379318 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0772538 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75263e+07, 1.75655e+07, 1.76021e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02694e+06, 5.10279e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.417 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.49377, 726.923 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2384.97, 704525 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.429, 212970 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1833.54, 491555 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.714, 0.00107185 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2241.26, 704525 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2384.97, 0 }, { 1257.1, 703243 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75076e+07, 1.752e+07, 1.7545e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00828e+06, 5.04569e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.59485, 222.173 } rm^3 +compflowStatistics, caprock: Phase mass: { 692.13, 215323 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 155.662, 65064.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 536.468, 150258 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.08932, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 684.04, 215323 } kg +compflowStatistics, caprock: Dissolved component mass: { { 692.13, 0 }, { 396.527, 214918 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.76967 +compflowStatistics: Max component CFL number: 0.628466 +Time: 4.84e+08s, dt:1e+06s, Cycle: 1378 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.73e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.73e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.05e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00378388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0714295 +coupledFlowAndWells: Time-step required will be decreased based on state change. +well_1Control: well is shut +compflowStatistics, reservoir: Pressure (min, average, max): 1.75256e+07, 1.75648e+07, 1.76015e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02628e+06, 5.10213e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.416 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.4884, 726.928 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2382.53, 704529 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.341, 212970 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1831.19, 491559 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.715, 0.00107184 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2238.81, 704529 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2382.53, 0 }, { 1257.4, 703247 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7507e+07, 1.75193e+07, 1.75444e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00762e+06, 5.04503e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.59832, 222.169 } rm^3 +compflowStatistics, caprock: Phase mass: { 693.602, 215319 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 155.904, 65064.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 537.697, 150254 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.32645, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 685.275, 215319 } kg +compflowStatistics, caprock: Dissolved component mass: { { 693.602, 0 }, { 397.2, 214914 } } kg +compflowStatistics: Max phase CFL number: 2.84528 +compflowStatistics: Max component CFL number: 0.634326 +Time: 4.85e+08s, dt:1e+06s, Cycle: 1379 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.40e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.40e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00377275 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0709169 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7525e+07, 1.75642e+07, 1.76008e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02562e+06, 5.10147e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.416 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.48304, 726.933 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2380.09, 704534 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.255, 212969 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1828.83, 491564 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.678, 0.00107184 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2236.41, 704534 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2380.09, 0 }, { 1257.7, 703251 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75063e+07, 1.75187e+07, 1.75437e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00696e+06, 5.04437e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.60179, 222.166 } rm^3 +compflowStatistics, caprock: Phase mass: { 695.072, 215316 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 156.15, 65064.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 538.922, 150251 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.55265, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 686.519, 215316 } kg +compflowStatistics, caprock: Dissolved component mass: { { 695.072, 0 }, { 397.872, 214910 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 2.97349 +compflowStatistics: Max component CFL number: 0.643136 +Time: 4.86e+08s, dt:1e+06s, Cycle: 1380 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.71e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.71e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.75e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.75e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.23e-06 ) ; + Last LinSolve(iter,res) = ( 6, 4.96e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00377012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736057 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75243e+07, 1.75635e+07, 1.76002e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02497e+06, 5.10081e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.415 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.47769, 726.937 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2377.65, 704538 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.169, 212969 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1826.48, 491569 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.677, 0.00107183 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2233.97, 704538 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2377.65, 0 }, { 1258, 703255 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75057e+07, 1.7518e+07, 1.75431e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00631e+06, 5.04371e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.768 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.60525, 222.162 } rm^3 +compflowStatistics, caprock: Phase mass: { 696.54, 215312 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 156.396, 65064.9 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 540.144, 150248 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.66986, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 687.87, 215312 } kg +compflowStatistics, caprock: Dissolved component mass: { { 696.54, 0 }, { 398.542, 214906 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.0947 +compflowStatistics: Max component CFL number: 0.657808 +Time: 4.87e+08s, dt:1e+06s, Cycle: 1381 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.02e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.39e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00376251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0754064 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75237e+07, 1.75628e+07, 1.75995e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02431e+06, 5.10016e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.415 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.47234, 726.942 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2375.22, 704542 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 551.081, 212969 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1824.14, 491573 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.659, 0.00107182 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2231.56, 704542 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2375.22, 0 }, { 1258.3, 703259 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7505e+07, 1.75174e+07, 1.75424e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00565e+06, 5.04306e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.6087, 222.159 } rm^3 +compflowStatistics, caprock: Phase mass: { 698.006, 215309 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 156.645, 65064.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 541.361, 150244 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 8.87637, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 689.129, 215309 } kg +compflowStatistics, caprock: Dissolved component mass: { { 698.006, 0 }, { 399.212, 214902 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.18567 +compflowStatistics: Max component CFL number: 0.674033 +Time: 4.88e+08s, dt:1e+06s, Cycle: 1382 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.20e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.20e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00374578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0704364 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7523e+07, 1.75622e+07, 1.75989e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02366e+06, 5.0995e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.414 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.46701, 726.947 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2372.79, 704547 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.994, 212969 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1821.8, 491578 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.69, 0.0010718 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2229.1, 704547 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2372.79, 0 }, { 1258.59, 703263 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75043e+07, 1.75167e+07, 1.75418e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.005e+06, 5.0424e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.61215, 222.155 } rm^3 +compflowStatistics, caprock: Phase mass: { 699.47, 215305 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 156.896, 65064.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 542.575, 150241 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.00174, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 690.469, 215305 } kg +compflowStatistics, caprock: Dissolved component mass: { { 699.47, 0 }, { 399.878, 214898 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.27223 +compflowStatistics: Max component CFL number: 0.690167 +Time: 4.89e+08s, dt:1e+06s, Cycle: 1383 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.88e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.88e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.35e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.35e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.07e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00373774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685712 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75224e+07, 1.75615e+07, 1.75982e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.023e+06, 5.09885e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.414 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.46168, 726.952 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2370.37, 704551 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.908, 212968 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1819.46, 491583 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.674, 0.00107181 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2226.69, 704551 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2370.37, 0 }, { 1258.89, 703268 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75037e+07, 1.75161e+07, 1.75411e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00435e+06, 5.04175e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.6156, 222.151 } rm^3 +compflowStatistics, caprock: Phase mass: { 700.933, 215302 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 157.15, 65064.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 543.784, 150237 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.21159, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 691.722, 215302 } kg +compflowStatistics, caprock: Dissolved component mass: { { 700.933, 0 }, { 400.542, 214893 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.35342 +compflowStatistics: Max component CFL number: 0.707529 +Time: 4.9e+08s, dt:1e+06s, Cycle: 1384 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.70e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.48e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.70e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.70e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.42e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00372024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633989 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75217e+07, 1.75609e+07, 1.75976e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02236e+06, 5.0982e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.413 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.45636, 726.957 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2367.95, 704556 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.826, 212968 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1817.12, 491587 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.65, 0.00107179 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2224.3, 704556 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2367.95, 0 }, { 1259.18, 703272 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.7503e+07, 1.75154e+07, 1.75405e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0037e+06, 5.0411e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.61905, 222.148 } rm^3 +compflowStatistics, caprock: Phase mass: { 702.395, 215299 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 157.407, 65064.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 544.988, 150234 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.41759, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 692.977, 215299 } kg +compflowStatistics, caprock: Dissolved component mass: { { 702.395, 0 }, { 401.205, 214889 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.39108 +compflowStatistics: Max component CFL number: 0.73268 +Time: 4.91e+08s, dt:1e+06s, Cycle: 1385 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.16e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.31e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.31e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.32e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00371307 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067756 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75211e+07, 1.75603e+07, 1.75969e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02171e+06, 5.09756e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.413 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.45106, 726.962 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2365.54, 704560 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.744, 212968 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1814.79, 491592 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.641, 0.00107176 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2221.9, 704560 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2365.54, 0 }, { 1259.47, 703276 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75024e+07, 1.75148e+07, 1.75398e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00305e+06, 5.04046e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.62249, 222.144 } rm^3 +compflowStatistics, caprock: Phase mass: { 703.854, 215295 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 157.666, 65064.8 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 546.187, 150230 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.65767, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 694.196, 215295 } kg +compflowStatistics, caprock: Dissolved component mass: { { 703.854, 0 }, { 401.868, 214885 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.38562 +compflowStatistics: Max component CFL number: 0.760215 +Time: 4.92e+08s, dt:1e+06s, Cycle: 1386 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.65e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 8.65e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.89e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00370613 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0707682 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75204e+07, 1.75596e+07, 1.75963e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02106e+06, 5.09691e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.412 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.44576, 726.967 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2363.13, 704564 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.659, 212968 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1812.47, 491597 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.621, 0.00107175 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2219.51, 704564 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2363.13, 0 }, { 1259.77, 703280 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75018e+07, 1.75141e+07, 1.75392e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.0024e+06, 5.03981e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.62592, 222.141 } rm^3 +compflowStatistics, caprock: Phase mass: { 705.311, 215292 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 157.929, 65064.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 547.382, 150227 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 9.88683, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 695.424, 215292 } kg +compflowStatistics, caprock: Dissolved component mass: { { 705.311, 0 }, { 402.528, 214881 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.39762 +compflowStatistics: Max component CFL number: 0.788953 +Time: 4.93e+08s, dt:1e+06s, Cycle: 1387 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.79e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.32e-06 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.32e-06 ) ; + Last LinSolve(iter,res) = ( 6, 5.02e-03 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.003691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668185 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75198e+07, 1.7559e+07, 1.75956e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.02042e+06, 5.09627e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.412 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.44047, 726.971 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2360.72, 704569 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.574, 212967 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1810.15, 491601 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.585, 0.00107174 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2217.14, 704569 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2360.72, 0 }, { 1260.06, 703284 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.75011e+07, 1.75135e+07, 1.75385e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00176e+06, 5.03917e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.767 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.62935, 222.137 } rm^3 +compflowStatistics, caprock: Phase mass: { 706.768, 215288 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 158.196, 65064.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 548.572, 150224 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.0985, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 696.669, 215288 } kg +compflowStatistics, caprock: Dissolved component mass: { { 706.768, 0 }, { 403.185, 214877 } } kg +compflowStatistics: Max phase CFL number: 3.40409 +compflowStatistics: Max component CFL number: 0.814623 +Time: 4.94e+08s, dt:1e+06s, Cycle: 1388 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.23e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.85e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.85e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.52e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00367469 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777767 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75191e+07, 1.75583e+07, 1.7595e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.01978e+06, 5.09563e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.411 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.43519, 726.976 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2358.32, 704573 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.489, 212967 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1807.83, 491606 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.547, 0.00107173 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2214.78, 704573 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2358.32, 0 }, { 1260.35, 703288 } } kg +well_1Control: well is shut +compflowStatistics, caprock: Pressure (min, average, max): 1.75005e+07, 1.75129e+07, 1.75379e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00112e+06, 5.03853e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.766 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.63279, 222.134 } rm^3 +compflowStatistics, caprock: Phase mass: { 708.223, 215285 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 158.465, 65064.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 549.758, 150220 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.3458, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 697.877, 215285 } kg +compflowStatistics, caprock: Dissolved component mass: { { 708.223, 0 }, { 403.839, 214873 } } kg +compflowStatistics: Max phase CFL number: 3.3967 +compflowStatistics: Max component CFL number: 0.835922 +Time: 4.95e+08s, dt:1e+06s, Cycle: 1389 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.77e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.88e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00366769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0773284 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75185e+07, 1.75577e+07, 1.75943e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.01914e+06, 5.09499e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.411 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.42992, 726.981 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2355.93, 704578 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.404, 212967 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1805.52, 491611 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.499, 0.00107169 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2212.43, 704578 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2355.93, 0 }, { 1260.64, 703292 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74998e+07, 1.75122e+07, 1.75373e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 5.00048e+06, 5.03789e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.766 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.63621, 222.13 } rm^3 +compflowStatistics, caprock: Phase mass: { 709.677, 215281 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 158.737, 65064.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 550.94, 150217 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.4989, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 699.178, 215281 } kg +compflowStatistics, caprock: Dissolved component mass: { { 709.677, 0 }, { 404.492, 214869 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.37532 +compflowStatistics: Max component CFL number: 0.852276 +Time: 4.96e+08s, dt:1e+06s, Cycle: 1390 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.15e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 5.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.93e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 7.93e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.13e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00366225 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0655059 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75179e+07, 1.75571e+07, 1.75937e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0185e+06, 5.09435e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.41 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.42466, 726.986 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2353.54, 704582 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.318, 212967 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1803.22, 491615 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.535, 0.00107166 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2210, 704582 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2353.54, 0 }, { 1260.92, 703296 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74992e+07, 1.75116e+07, 1.75366e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.99984e+06, 5.03725e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.766 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.63964, 222.126 } rm^3 +compflowStatistics, caprock: Phase mass: { 711.129, 215278 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 159.007, 65064.7 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 552.121, 150213 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.5144, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 700.614, 215278 } kg +compflowStatistics, caprock: Dissolved component mass: { { 711.129, 0 }, { 405.143, 214865 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.33526 +compflowStatistics: Max component CFL number: 0.862689 +Time: 4.97e+08s, dt:1e+06s, Cycle: 1391 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.13e-03 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.13e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.28e-07 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 6.28e-07 ) ; + Last LinSolve(iter,res) = ( 8, 9.95e-04 ) ; +well_1Control: well is shut +compositionalMultiphaseFlow: Max relative pressure change: 0.00365062 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0704386 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75172e+07, 1.75564e+07, 1.75931e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.01787e+06, 5.09371e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.41 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.41941, 726.991 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2351.15, 704586 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.231, 212967 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1800.92, 491620 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.485, 0.00107166 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2207.66, 704586 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2351.15, 0 }, { 1261.21, 703300 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74986e+07, 1.75109e+07, 1.7536e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.99921e+06, 5.03661e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.766 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.64306, 222.123 } rm^3 +compflowStatistics, caprock: Phase mass: { 712.579, 215275 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 159.281, 65064.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 553.298, 150210 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.7788, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 701.8, 215275 } kg +compflowStatistics, caprock: Dissolved component mass: { { 712.579, 0 }, { 405.792, 214861 } } kg +compflowStatistics: Max phase CFL number: 3.26975 +compflowStatistics: Max component CFL number: 0.865271 +Time: 4.98e+08s, dt:1e+06s, Cycle: 1392 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.00e-05 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 9.00e-05 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00362831 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695889 +coupledFlowAndWells: Time-step required will be increased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.75166e+07, 1.75558e+07, 1.75925e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.01723e+06, 5.09308e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.41 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.41417, 726.995 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2348.77, 704591 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.143, 212966 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1798.63, 491624 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.472, 0.00107167 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2205.3, 704591 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2348.77, 0 }, { 1261.5, 703304 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74979e+07, 1.75103e+07, 1.75354e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.99857e+06, 5.03598e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.766 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.64648, 222.119 } rm^3 +compflowStatistics, caprock: Phase mass: { 714.03, 215271 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 159.559, 65064.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 554.471, 150207 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 10.9722, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 703.058, 215271 } kg +compflowStatistics, caprock: Dissolved component mass: { { 714.03, 0 }, { 406.434, 214857 } } kg +well_1Control: well is shut +compflowStatistics: Max phase CFL number: 3.16525 +compflowStatistics: Max component CFL number: 0.858633 +Time: 4.99e+08s, dt:1e+06s, Cycle: 1393 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.98e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 4.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-04 ) ; ( Rwell ) = ( 0.00e+00 ) ; ( R ) = ( 2.69e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.85e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 0.00360957 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0725053 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.7516e+07, 1.75552e+07, 1.75918e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 5.0166e+06, 5.09245e+06 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 732.409 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 5.40894, 727 } rm^3 +compflowStatistics, reservoir: Phase mass: { 2346.39, 704595 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 550.057, 212966 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 1796.33, 491629 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 143.424, 0.00107168 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 2202.97, 704595 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 2346.39, 0 }, { 1261.79, 703309 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.74973e+07, 1.75097e+07, 1.75347e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 4.99794e+06, 5.03535e+06 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 223.766 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 1.6499, 222.116 } rm^3 +compflowStatistics, caprock: Phase mass: { 715.481, 215268 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 159.842, 65064.6 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 555.639, 150203 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 11.2128, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 704.269, 215268 } kg +compflowStatistics, caprock: Dissolved component mass: { { 715.481, 0 }, { 407.073, 214853 } } kg +compflowStatistics: Max phase CFL number: 2.99932 +compflowStatistics: Max component CFL number: 0.84439 +Cleaning up events +well_1Control: well is shut +Umpire HOST sum across ranks: 22.3 GB +Umpire HOST rank max: 56.4 MB +total time 4988.354s +initialization time 100.788s +run time 4823.863s diff --git a/geos-posp/tests/Data/small_job_GEOS_246861.out b/geos-posp/tests/Data/small_job_GEOS_246861.out new file mode 100644 index 00000000..d6270ac1 --- /dev/null +++ b/geos-posp/tests/Data/small_job_GEOS_246861.out @@ -0,0 +1,303 @@ +GEOSX version: 0.2.0 (HEAD, sha1: c40be5d) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.26.0 +Adding Solver of type CompositionalMultiphaseReservoir, named compositionalMultiphaseReservoirSolver +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFVMSolver +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWellSolver +Adding Mesh: VTKMesh, mesh +Adding Mesh: InternalWell, wellInjector +Adding Event: PeriodicEvent, outputInjectionPeriod +Adding Event: PeriodicEvent, outputPostInjectionPeriod +Adding Event: PeriodicEvent, statistics +Adding Event: SoloEvent, soloStatistics +Adding Event: PeriodicEvent, solverApplicationInjectionPeriod +Adding Event: PeriodicEvent, solverApplicationPostInjectionPeriod1 +Adding Event: PeriodicEvent, solverApplicationPostInjectionPeriod2 +Adding Output: VTK, vtkOutput + TableFunction: initGasCompFracTable + TableFunction: initWaterCompFracTable + TableFunction: initTempTable + TableFunction: waterRelativePermeabilityTable + TableFunction: gasRelativePermeabilityTable + TableFunction: totalRateTable +Adding Object CellElementRegion named reservoir from ObjectManager::Catalog. +Adding Object CellElementRegion named reservoir_admunsen from ObjectManager::Catalog. +Adding Object WellElementRegion named well from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_EzrokhiBrineDensity_sat_density_table + TableFunction: fluid_phaseModel1_EzrokhiBrineDensity_sat_pressure_table + TableFunction: fluid_phaseModel1_EzrokhiBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table +VTK `vtkOutput`: found 8 fields to plot in `fieldNames`. These fields will be output regardless of the `plotLevel` specified by the user. No other field will be output. + TableFunction: wellControls_ConstantBHP_table + TableFunction: wellControls_ConstantPhaseRate_table +VTKMesh 'mesh': reading mesh from /work206/workrd/users/j0459652/GEOSX/nl_hexdom_margaux/04_hexdom_10m_with_uvw_with_properties_from_structured_grid_reservoir.vtu +Generating global Ids from VTK mesh +VTKMesh 'mesh': generating GEOSX mesh data structure +Number of nodes: 715020 + Number of elems: 475821 + C3D4: 705248 + C3D5: 221014 + C3D8: 475821 +Load balancing: min avg max +(element/rank): 421 4956 15051 + +++++++++++++++++++++++++++ +InternalWellGenerator = wellInjector +MPI rank = 0 + +Number of well elements = 16 +Well element #0 +Coordinates of the element center: { 524560, 6.71631e+06, -2606.5 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 524560, 6.71631e+06, -2618 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 524560, 6.71631e+06, -2628 } +Next well element # = 1 +Previous well element #3 +First well node: #2 +Second well node: #3 +Well element #3 +Coordinates of the element center: { 524560, 6.71631e+06, -2638 } +Next well element # = 2 +Previous well element #4 +First well node: #3 +Second well node: #4 +Well element #4 +Coordinates of the element center: { 524560, 6.71631e+06, -2648 } +Next well element # = 3 +Previous well element #5 +First well node: #4 +Second well node: #5 +Well element #5 +Coordinates of the element center: { 524560, 6.71631e+06, -2658 } +Next well element # = 4 +Previous well element #6 +First well node: #5 +Second well node: #6 +Well element #6 +Coordinates of the element center: { 524560, 6.71631e+06, -2668 } +Next well element # = 5 +Previous well element #7 +First well node: #6 +Second well node: #7 +Well element #7 +Coordinates of the element center: { 524560, 6.71631e+06, -2678 } +Next well element # = 6 +Previous well element #8 +First well node: #7 +Second well node: #8 +Well element #8 +Coordinates of the element center: { 524560, 6.71631e+06, -2688 } +Next well element # = 7 +Previous well element #9 +First well node: #8 +Second well node: #9 +Well element #9 +Coordinates of the element center: { 524560, 6.71631e+06, -2698 } +Next well element # = 8 +Previous well element #10 +First well node: #9 +Second well node: #10 +Well element #10 +Coordinates of the element center: { 524560, 6.71631e+06, -2708 } +Next well element # = 9 +Previous well element #11 +First well node: #10 +Second well node: #11 +Well element #11 +Coordinates of the element center: { 524560, 6.71631e+06, -2718 } +Next well element # = 10 +Previous well element #12 +First well node: #11 +Second well node: #12 +Well element #12 +Coordinates of the element center: { 524560, 6.71631e+06, -2728 } +Next well element # = 11 +Previous well element #13 +First well node: #12 +Second well node: #13 +Well element #13 +Coordinates of the element center: { 524560, 6.71631e+06, -2738 } +Next well element # = 12 +Previous well element #14 +First well node: #13 +Second well node: #14 +Well element #14 +Coordinates of the element center: { 524560, 6.71631e+06, -2748 } +Next well element # = 13 +Previous well element #15 +First well node: #14 +Second well node: #15 +Well element #15 +Coordinates of the element center: { 524560, 6.71631e+06, -2758 } +Next well element # = 14 +No previous well element +First well node: #15 +Second well node: #16 + +Number of perforations = 16 +Perforation #0 +Coordinates of the perforation: { 524560, 6.71631e+06, -2610.5 } +Is connected to well element #0 +Perforation #1 +Coordinates of the perforation: { 524560, 6.71631e+06, -2619.5 } +Is connected to well element #1 +Perforation #2 +Coordinates of the perforation: { 524560, 6.71631e+06, -2628.5 } +Is connected to well element #2 +Perforation #3 +Coordinates of the perforation: { 524560, 6.71631e+06, -2637.9 } +Is connected to well element #3 +Perforation #4 +Coordinates of the perforation: { 524560, 6.71631e+06, -2647 } +Is connected to well element #4 +Perforation #5 +Coordinates of the perforation: { 524560, 6.71631e+06, -2656.5 } +Is connected to well element #5 +Perforation #6 +Coordinates of the perforation: { 524560, 6.71631e+06, -2666.5 } +Is connected to well element #6 +Perforation #7 +Coordinates of the perforation: { 524560, 6.71631e+06, -2676.5 } +Is connected to well element #7 +Perforation #8 +Coordinates of the perforation: { 524560, 6.71631e+06, -2686.5 } +Is connected to well element #8 +Perforation #9 +Coordinates of the perforation: { 524560, 6.71631e+06, -2696.5 } +Is connected to well element #9 +Perforation #10 +Coordinates of the perforation: { 524560, 6.71631e+06, -2706.5 } +Is connected to well element #10 +Perforation #11 +Coordinates of the perforation: { 524560, 6.71631e+06, -2716.5 } +Is connected to well element #11 +Perforation #12 +Coordinates of the perforation: { 524560, 6.71631e+06, -2726.3 } +Is connected to well element #12 +Perforation #13 +Coordinates of the perforation: { 524560, 6.71631e+06, -2736.3 } +Is connected to well element #13 +Perforation #14 +Coordinates of the perforation: { 524560, 6.71631e+06, -2746.3 } +Is connected to well element #14 +Perforation #15 +Coordinates of the perforation: { 524560, 6.71631e+06, -2756.3 } +Is connected to well element #15 + +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_hexahedra +mesh/Level0/reservoir/2_hexahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_pyramids +mesh/Level0/reservoir/2_pyramids/rock allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_tetrahedra +mesh/Level0/reservoir/2_tetrahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_hexahedra +mesh/Level0/reservoir/3_hexahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_pyramids +mesh/Level0/reservoir/3_pyramids/rock allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_tetrahedra +mesh/Level0/reservoir/3_tetrahedra/rock allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, well, wellUniqueSubRegion +mesh/Level0/well/wellUniqueSubRegion/fluid allocated 1 quadrature points +mesh/Level0/well/wellUniqueSubRegion/relperm allocated 1 quadrature points + TableFunction: equil_2_hexahedra_water_table + TableFunction: equil_2_tetrahedra_water_table + TableFunction: equil_2_pyramids_water_table + TableFunction: equil_3_hexahedra_water_table + TableFunction: equil_3_tetrahedra_water_table + TableFunction: equil_3_pyramids_water_table +Time: 0s, dt:8600s, Cycle: 0 +compflowStatistics, reservoir: Pressure (min, average, max): 2.0159e+07, 2.68032e+07, 3.89368e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 346.964, 372.107, 395.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 3.45705e+10 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 0, 3.45705e+10 } rm^3 +compflowStatistics, reservoir: Phase mass (including both trapped and non-trapped): { 0, 3.35481e+13 } kg +compflowStatistics, reservoir: Trapped phase mass: { 0, 1.00644e+13 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 0, 0 }, { 0, 3.35481e+13 } } kg + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 3.12e+02 ) ; ( R ) = ( 3.12e+02 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 1 | Final Rel Res: 5.96636e-05 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 1.5156 s | Solve Time: 0.041093 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-04 ) ; ( Rwell ) = ( 3.49e-04 ) ; ( R ) = ( 6.01e-04 ) ; + Last LinSolve(iter,res) = ( 1, 5.97e-05 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0884298 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 6.29211e-09 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 8600s, dt:17124.3s, Cycle: 1 +wellControls: BHP (at the specified reference elevation): 27452073.075918034 Pa +wellControls: Total rate: 49.49343235863489 kg/s; total surface volumetric rate: 26.524664060614963 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.52466406061294 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0274305932361715e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 3.60e-04 ) ; ( R ) = ( 4.91e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.00144374 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.327855 s | Solve Time: 0.0461692 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 4.13e-06 ) ; ( R ) = ( 3.10e-05 ) ; + Last LinSolve(iter,res) = ( 2, 1.44e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0487591 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 2.10852e-08 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +Time: 25724.3s, dt:34165.3s, Cycle: 2 +wellControls: BHP (at the specified reference elevation): 27375394.375235207 Pa +wellControls: Total rate: 49.485508293503074 kg/s; total surface volumetric rate: 26.5204173726081 sm3/s +wellControls: Phase 0 surface volumetric rate: 26.520417372606076 sm3/s +wellControls: Phase 1 surface volumetric rate: 2.0271059947731947e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.13e-03 ) ; ( Rwell ) = ( 4.14e-06 ) ; ( R ) = ( 8.13e-03 ) ; +{ 3, 4 } + Linear Solver | Success | Iterations: 2 | Final Rel Res: 0.0019764 | Make Restrictor Time: 0 | Compute Auu Time: 0 | SC Filter Time: 0 | Setup Time: 0.336642 s | Solve Time: 0.0473239 s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.33e-04 ) ; ( Rwell ) = ( 6.43e-06 ) ; ( R ) = ( 1.33e-04 ) ; + Last LinSolve(iter,res) = ( 2, 1.98e-03 ) ; +compositionalMultiphaseFVMSolver: Max relative pressure change: 0.0263923 % +compositionalMultiphaseFVMSolver: Max absolute phase volume fraction change: 8.11139e-08 +compositionalMultiphaseReservoirSolver: Time-step required will be increased based on state change. +compositionalMultiphaseReservoirSolver, number of time steps: 767 +compositionalMultiphaseReservoirSolver, number of successful nonlinear iterations: 2519 +compositionalMultiphaseReservoirSolver, number of successful linear iterations: 14336 +compositionalMultiphaseReservoirSolver, number of time step cuts: 0 +compositionalMultiphaseReservoirSolver, number of discarded nonlinear iterations: 0 +compositionalMultiphaseReservoirSolver, number of discarded linear iterations: 0 +Umpire HOST sum across ranks: 7.2 GB +Umpire HOST rank max: 98.7 MB +total time 1385.860s +initialization time 120.890s +run time 1263.686s diff --git a/geos-posp/tests/Data/small_job_GEOS_642571.out b/geos-posp/tests/Data/small_job_GEOS_642571.out new file mode 100644 index 00000000..02ec7b64 --- /dev/null +++ b/geos-posp/tests/Data/small_job_GEOS_642571.out @@ -0,0 +1,245 @@ +Num ranks: 250 +MKL max threads: 1 +GEOSX version: 0.2.0 (feature/dkachuma/allow-negative-pressure-with-errors, sha1: d15a5d5) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Started at 2023-06-09 16:18:46 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, SyntheticMesh +Adding Mesh: InternalWell, well_1 +Adding Geometric Object: Box, aquifer1 +Adding Geometric Object: Box, aquifer2 +Adding Geometric Object: Box, aquifer3 +Adding Geometric Object: Box, aquifer4 +Adding Event: PeriodicEvent, outputInjectionPeriod +Adding Event: PeriodicEvent, outputPostInjectionPeriod +Adding Event: PeriodicEvent, statistics +Adding Event: PeriodicEvent, solverApplicationsInjectionPeriod +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod1 +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod2 +Adding Output: VTK, vtkOutputReference + TableFunction: WATVD + TableFunction: CO2VD + TableFunction: TEMPVD + TableFunction: totalRateTable + TableFunction: RELPERM.KRW + TableFunction: RELPERM.KRG.DRAINAGE + TableFunction: RELPERM.KRG.IMBIBITION +Adding Object CellElementRegion named Reservoir from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: aquifer1_pressureInfluence_table + TableFunction: aquifer2_pressureInfluence_table + TableFunction: aquifer3_pressureInfluence_table + TableFunction: aquifer4_pressureInfluence_table + TableFunction: wellControls_ConstantBHP_table + TableFunction: wellControls_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table +VTKMesh 'SyntheticMesh': reading mesh from /work206/workrd/users/l1092630/Test_Raymond_structuré/ReferenceMesh.vtu +Generating global Ids from VTK mesh +VTKMesh 'SyntheticMesh': generating GEOSX mesh data structure +Importing cell block hexahedra +Number of nodes: 8200851 + Number of elems: 8000000 + C3D8: 8000000 +Load balancing: min avg max +(element/rank): 26230 32000 33498 +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Reservoir, hexahedra +SyntheticMesh/Level0/Reservoir/hexahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/hexahedra/rock_reservoir allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion, wellRegionUniqueSubRegion +SyntheticMesh/Level0/wellRegion/wellRegionUniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion/wellRegionUniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh: importing field data from mesh dataset +Rank 177: Perforation at (2586610,33512700,3045); perforated element center: (2586633.375,33512713,3045.7802124023438); transmissibility: 2.3771304734308088e-12 Pa.s.rm^3/s/Pa + TableFunction: INITIALISATION_hexahedra_water_table +Time: 0s, dt:100s, Cycle: 0 +compflowStatistics, Reservoir: Pressure (min, average, max): 2.86419e+07, 2.93341e+07, 3.006e+07 Pa +compflowStatistics, Reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, Reservoir: Temperature (min, average, max): 366.483, 366.483, 366.483 K +compflowStatistics, Reservoir: Total dynamic pore volume: 1.00462e+11 rm^3 +compflowStatistics, Reservoir: Phase dynamic pore volumes: { 0, 1.00462e+11 } rm^3 +compflowStatistics, Reservoir: Phase mass: { 0, 9.83123e+13 } kg +compflowStatistics, Reservoir: Trapped phase mass (metric 1): { 0, 3.24431e+13 } kg +compflowStatistics, Reservoir: Non-trapped phase mass (metric 1): { 0, 6.58692e+13 } kg +compflowStatistics, Reservoir: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 0, 9.83123e+13 } kg +compflowStatistics, Reservoir: Dissolved component mass: { { 0, 0 }, { 0, 9.83123e+13 } } kg +compflowStatistics: Max phase CFL number: 8.16102e-11 +compflowStatistics: Max component CFL number: 8.16102e-11 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 0 kg/s, which corresponds to a total surface volumetric rate of 0 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 0 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 0 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 31711363.90586692 Pa +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 18290.4251297056 kg/s, which corresponds to a total surface volumetric rate of 9790.274374448885 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 9790.274374448149 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 7.367585776885482e-10 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 31711363.90586692 Pa +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 100s, the boundary condition 'aquifer1' is applied to the face set 'aquifer1' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 14692. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 100s, the boundary condition 'aquifer2' is applied to the face set 'aquifer2' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 19998. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 100s, the boundary condition 'aquifer3' is applied to the face set 'aquifer3' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 14220. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 100s, the boundary condition 'aquifer4' is applied to the face set 'aquifer4' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 19998. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 3.77e+02 ) ; ( R ) = ( 3.77e+02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 48.32778944100937 kg/s, which corresponds to a total surface volumetric rate of 25.86830624126073 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 25.868306241258782 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 1.9466968733035026e-12 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 37094617.068262696 Pa + ( Rflow ) = ( 1.91e-05 ) ; ( Rwell ) = ( 1.29e-04 ) ; ( R ) = ( 1.31e-04 ) ; + Last LinSolve(iter,res) = ( 1, 1.11e-04 ) ; +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 100s, the boundary condition 'aquifer1' produces a flux of -0.6181975187076816 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 100s, the boundary condition 'aquifer2' produces a flux of -0.6180843994083122 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 100s, the boundary condition 'aquifer3' produces a flux of -0.618090355732848 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 100s, the boundary condition 'aquifer4' produces a flux of -0.6181996097752541 kg (or moles if useMass=0). +compositionalMultiphaseFlow: Max relative pressure change: 0.076635 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 1.90681e-08 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 100s, dt:200s, Cycle: 1 +wellControls: BHP (at the specified reference elevation): 37094617.068262696 Pa +wellControls: Total rate: 48.32778944100937 kg/s; total surface volumetric rate: 25.86830624126073 sm3/s +wellControls: Phase 0 surface volumetric rate: 25.868306241258782 sm3/s +wellControls: Phase 1 surface volumetric rate: 1.9466968733035026e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 48.32778944100937 kg/s, which corresponds to a total surface volumetric rate of 25.86830624126073 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 25.868306241258782 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 1.9466968733035026e-12 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 37094617.068262696 Pa +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 300s, the boundary condition 'aquifer1' is applied to the face set 'aquifer1' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 14692. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 300s, the boundary condition 'aquifer2' is applied to the face set 'aquifer2' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 19998. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 300s, the boundary condition 'aquifer3' is applied to the face set 'aquifer3' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 14220. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 300s, the boundary condition 'aquifer4' is applied to the face set 'aquifer4' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 19998. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. + ( Rflow ) = ( 8.15e-04 ) ; ( Rwell ) = ( 8.66e-05 ) ; ( R ) = ( 8.19e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 48.3273106298979 kg/s, which corresponds to a total surface volumetric rate of 25.86804994912309 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 25.868049949121144 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 1.9466775862619354e-12 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 36934158.13373236 Pa + ( Rflow ) = ( 2.24e-06 ) ; ( Rwell ) = ( 6.04e-07 ) ; ( R ) = ( 2.32e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.35e-03 ) ; +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 300s, the boundary condition 'aquifer1' produces a flux of -0.9277628658291136 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 300s, the boundary condition 'aquifer2' produces a flux of -0.9275930970753377 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 300s, the boundary condition 'aquifer3' produces a flux of -0.9276020230175535 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 300s, the boundary condition 'aquifer4' produces a flux of -0.9277658630941507 kg (or moles if useMass=0). +compositionalMultiphaseFlow: Max relative pressure change: 0.0510061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 7.51713e-08 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 300s, dt:400s, Cycle: 2 +wellControls: BHP (at the specified reference elevation): 36934158.13373236 Pa +wellControls: Total rate: 48.3273106298979 kg/s; total surface volumetric rate: 25.86804994912309 sm3/s +wellControls: Phase 0 surface volumetric rate: 25.868049949121144 sm3/s +wellControls: Phase 1 surface volumetric rate: 1.9466775862619354e-12 sm3/s + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 48.3273106298979 kg/s, which corresponds to a total surface volumetric rate of 25.86804994912309 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 25.868049949121144 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 1.9466775862619354e-12 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 36934158.13373236 Pa +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 700s, the boundary condition 'aquifer1' is applied to the face set 'aquifer1' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 14692. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 700s, the boundary condition 'aquifer2' is applied to the face set 'aquifer2' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 19998. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 700s, the boundary condition 'aquifer3' is applied to the face set 'aquifer3' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 14220. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. +CompositionalMultiphaseFVM compositionalMultiphaseFlow: at time 700s, the boundary condition 'aquifer4' is applied to the face set 'aquifer4' in 'faceManager'. +The scale of this boundary condition is 0 and multiplies the value of the provided function (if any). +The total number of target faces (including ghost faces) is 19998. +Note that if this number is equal to zero, the boundary condition will not be applied on this face set. + ( Rflow ) = ( 1.58e-03 ) ; ( Rwell ) = ( 3.25e-06 ) ; ( R ) = ( 1.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 +Rank 177: wellControls: surface density computed with P_surface = 101325 Pa and T_surface = 288.71 K +Rank 177: wellControls: The total fluid density at surface conditions is 1.8682239567708956 kg/sm3. +The total rate is 48.32731072494112 kg/s, which corresponds to a total surface volumetric rate of 25.868049999996657 sm3/s +Rank 177: wellControls: The density of phase 0 at surface conditions is 1.868223956694465 kg/sm3. +The phase surface volumetric rate is 25.86804999999471 sm3/s +Rank 177: wellControls: The density of phase 1 at surface conditions is 1017.5050421623865 kg/sm3. +The phase surface volumetric rate is 1.946677590090179e-12 sm3/s +Rank 177: wellControls: BHP (at the specified reference elevation): 36936280.88209122 Pa + ( Rflow ) = ( 3.39e-06 ) ; ( Rwell ) = ( 2.72e-09 ) ; ( R ) = ( 3.39e-06 ) ; + Last LinSolve(iter,res) = ( 3, 3.57e-03 ) ; +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 700s, the boundary condition 'aquifer1' produces a flux of -1.5571182320345898 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 700s, the boundary condition 'aquifer2' produces a flux of -1.5568332821949953 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 700s, the boundary condition 'aquifer3' produces a flux of -1.55684825159388 kg (or moles if useMass=0). +FlowSolverBase compositionalMultiphaseFlow (SimuDeck_aquifer_pression_meme.xml, l.28): at time 700s, the boundary condition 'aquifer4' produces a flux of -1.5571231793720164 kg (or moles if useMass=0). +compositionalMultiphaseFlow: Max relative pressure change: 0.0438584 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 2.97145e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Umpire HOST sum across ranks: 48.5 GB +Umpire HOST rank max: 219.2 MB +Finished at 2023-06-09 20:09:54 +total time 03:51:08.108 +initialization time 00:08:32.981 +run time 03:41:33.966 diff --git a/geos-posp/tests/Data/small_job_GEOS_825200.out b/geos-posp/tests/Data/small_job_GEOS_825200.out new file mode 100644 index 00000000..7a1d0055 --- /dev/null +++ b/geos-posp/tests/Data/small_job_GEOS_825200.out @@ -0,0 +1,8992 @@ +Num ranks: 1 +MKL max threads: 1 +GEOSX version: 0.2.0 (feature/dkachuma/allow-negative-pressure-with-errors, sha1: d15a5d5) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Started at 2023-06-20 16:04:54 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, SyntheticMesh +Adding Mesh: InternalWell, well_1 +Adding Mesh: InternalWell, well_2 +Adding Mesh: InternalWell, well_3 +Adding Event: PeriodicEvent, outputInjectionPeriod +Adding Event: PeriodicEvent, outputPostInjectionPeriod +Adding Event: PeriodicEvent, statistics +Adding Event: PeriodicEvent, solverApplicationsInjectionPeriod +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod1 +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod2 +Adding Output: VTK, vtkOutput + TableFunction: totalRateTable +Adding Object CellElementRegion named Reservoir from ObjectManager::Catalog. +Adding Object CellElementRegion named Caprock from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion1 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion2 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion3 from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: wellControls1_ConstantBHP_table + TableFunction: wellControls1_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table + TableFunction: wellControls2_ConstantBHP_table + TableFunction: wellControls2_ConstantPhaseRate_table + TableFunction: wellControls3_ConstantBHP_table + TableFunction: wellControls3_ConstantPhaseRate_table +VTKMesh 'SyntheticMesh': reading mesh from /scratchrd/GIS/OT/l1094441/TestJeanne/TestJeanne9C/ModelA.vtu +Generating global Ids from VTK mesh +VTKMesh 'SyntheticMesh': generating GEOSX mesh data structure +Importing cell block 0_tetrahedra +Importing cell block 3_tetrahedra +Importing cell block 1_tetrahedra +Importing cell block 4_tetrahedra +Importing cell block 2_tetrahedra +Number of nodes: 9188 + Number of elems: 48935 + C3D4: 48935 +Load balancing: min avg max +(element/rank): 48935 48935 48935 + +++++++++++++++++++++++++++ +InternalWellGenerator = well_1 +MPI rank = 0 + +Number of well elements = 3 +Well element #0 +Coordinates of the element center: { 400, 1400, 237.313 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 400, 1400, -79.354 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 400, 1400, -396.021 } +Next well element # = 1 +No previous well element +First well node: #2 +Second well node: #3 + +Number of perforations = 3 +Perforation #0 +Coordinates of the perforation: { 400, 1400, -15 } +Is connected to well element #1 +Perforation #1 +Coordinates of the perforation: { 400, 1400, -120.436 } +Is connected to well element #1 +Perforation #2 +Coordinates of the perforation: { 400, 1400, -350 } +Is connected to well element #2 + + +++++++++++++++++++++++++++ +InternalWellGenerator = well_2 +MPI rank = 0 + +Number of well elements = 2 +Well element #0 +Coordinates of the element center: { 1200, 742.759, 158.146 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 1200, 742.759, -316.854 } +Next well element # = 0 +No previous well element +First well node: #1 +Second well node: #2 + +Number of perforations = 2 +Perforation #0 +Coordinates of the perforation: { 1200, 742.759, 100 } +Is connected to well element #0 +Perforation #1 +Coordinates of the perforation: { 1200, 742.759, -500 } +Is connected to well element #1 + + +++++++++++++++++++++++++++ +InternalWellGenerator = well_3 +MPI rank = 0 + +Number of well elements = 5 +Well element #0 +Coordinates of the element center: { 800, 1450, 300.646 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 800, 1450, 110.646 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 800, 1450, -79.354 } +Next well element # = 1 +Previous well element #3 +First well node: #2 +Second well node: #3 +Well element #3 +Coordinates of the element center: { 800, 1450, -269.354 } +Next well element # = 2 +Previous well element #4 +First well node: #3 +Second well node: #4 +Well element #4 +Coordinates of the element center: { 800, 1450, -459.354 } +Next well element # = 3 +No previous well element +First well node: #4 +Second well node: #5 + +Number of perforations = 5 +Perforation #0 +Coordinates of the perforation: { 800, 1450, 150 } +Is connected to well element #1 +Perforation #1 +Coordinates of the perforation: { 800, 1450, -30 } +Is connected to well element #2 +Perforation #2 +Coordinates of the perforation: { 800, 1450, -150 } +Is connected to well element #2 +Perforation #3 +Coordinates of the perforation: { 800, 1450, -325 } +Is connected to well element #3 +Perforation #4 +Coordinates of the perforation: { 800, 1450, -480 } +Is connected to well element #4 + +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Caprock, 4_tetrahedra +SyntheticMesh/Level0/Caprock/4_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Caprock/4_tetrahedra/rock_caprock allocated 1 quadrature points +SyntheticMesh/Level0/Caprock/4_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Overburden, 3_tetrahedra +SyntheticMesh/Level0/Overburden/3_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Overburden/3_tetrahedra/rock_burden allocated 1 quadrature points +SyntheticMesh/Level0/Overburden/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Reservoir, 2_tetrahedra +SyntheticMesh/Level0/Reservoir/2_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/2_tetrahedra/rock_reservoir allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Salt, 0_tetrahedra +SyntheticMesh/Level0/Salt/0_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Salt/0_tetrahedra/rock_salt allocated 1 quadrature points +SyntheticMesh/Level0/Salt/0_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Underburden, 1_tetrahedra +SyntheticMesh/Level0/Underburden/1_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Underburden/1_tetrahedra/rock_burden allocated 1 quadrature points +SyntheticMesh/Level0/Underburden/1_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion1, wellRegion1UniqueSubRegion +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion2, wellRegion2UniqueSubRegion +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion3, wellRegion3UniqueSubRegion +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +SyntheticMesh: importing field data from mesh dataset +Time: 0s, dt:100s, Cycle: 0 +compflowStatistics, Reservoir: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 0, 6.38235e+10 } kg +compflowStatistics, Caprock: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 0, 1.25037e+10 } kg +compflowStatistics: Max phase CFL number: 0.00696878 +compflowStatistics: Max component CFL number: 0.00696878 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.54e+02 ) ; ( R ) = ( 1.54e+02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 7.41e-01 ) ; ( R ) = ( 7.41e-01 ) ; + Last LinSolve(iter,res) = ( 1, 9.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.70e-05 ) ; ( Rwell ) = ( 9.97e-04 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 2, 4.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12337146.157562563 Pa +wellControls1: Total rate: 56.37348443784919 kg/s; total surface volumetric rate: 30.024025669350802 sm3/s +wellControls1: Phase 0 surface volumetric rate: 30.023748128796043 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027754055475897704 sm3/s +wellControls2: BHP (at the specified reference elevation): 13268440.020500632 Pa +wellControls2: Total rate: 56.38455514210006 kg/s; total surface volumetric rate: 30.029921829787227 sm3/s +wellControls2: Phase 0 surface volumetric rate: 30.029644234728664 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002775950585639181 sm3/s +wellControls3: BHP (at the specified reference elevation): 12318458.650753867 Pa +wellControls3: Total rate: 56.379144772078966 kg/s; total surface volumetric rate: 30.027040313946728 sm3/s +wellControls3: Phase 0 surface volumetric rate: 30.02676274552475 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002775684219790799 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.40959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 5.78676e-09 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 100s, dt:200s, Cycle: 1 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 8.49e-04 ) ; ( Rwell ) = ( 9.97e-04 ) ; ( R ) = ( 1.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.24e-05 ) ; ( Rwell ) = ( 3.96e-06 ) ; ( R ) = ( 9.24e-05 ) ; + Last LinSolve(iter,res) = ( 3, 2.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12310196.482923582 Pa +wellControls1: Total rate: 56.3283651953819 kg/s; total surface volumetric rate: 29.999995554705098 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.99971823628349 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731842161056295 sm3/s +wellControls2: BHP (at the specified reference elevation): 13283621.245611288 Pa +wellControls2: Total rate: 56.328363147049984 kg/s; total surface volumetric rate: 29.999994463781402 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.99971714536988 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184115261253 sm3/s +wellControls3: BHP (at the specified reference elevation): 12227845.268549167 Pa +wellControls3: Total rate: 56.32836414809141 kg/s; total surface volumetric rate: 29.999994996927327 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999717678510873 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184164545015 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.15934 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 1.03308e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 300s, dt:400s, Cycle: 2 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.64e-03 ) ; ( Rwell ) = ( 4.97e-06 ) ; ( R ) = ( 1.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 5.63e-06 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 3, 6.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12321245.117079774 Pa +wellControls1: Total rate: 56.32837354181888 kg/s; total surface volumetric rate: 29.999999999944567 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681481867 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270213385 sm3/s +wellControls2: BHP (at the specified reference elevation): 13381898.728875142 Pa +wellControls2: Total rate: 56.32837354179333 kg/s; total surface volumetric rate: 29.999999999930964 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681468263 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627020005 sm3/s +wellControls3: BHP (at the specified reference elevation): 12261492.207801165 Pa +wellControls3: Total rate: 56.32837354180582 kg/s; total surface volumetric rate: 29.999999999937614 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.99972268147491 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627020722 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.53908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 2.93995e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 700s, dt:800s, Cycle: 3 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.22e-03 ) ; ( Rwell ) = ( 5.63e-06 ) ; ( R ) = ( 3.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.05e-05 ) ; ( Rwell ) = ( 3.22e-06 ) ; ( R ) = ( 3.06e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12362535.831335485 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13510729.712916294 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12317848.1586993 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 3.20584 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 9.42513e-07 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1500s, dt:1600s, Cycle: 4 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-03 ) ; ( Rwell ) = ( 5.40e-06 ) ; ( R ) = ( 6.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.50e-04 ) ; ( Rwell ) = ( 5.73e-06 ) ; ( R ) = ( 3.50e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12459883.312855111 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13654363.938479979 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12398787.671024375 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 4.06388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 2.83724e-06 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3100s, dt:3200s, Cycle: 5 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 6.86e-06 ) ; ( R ) = ( 1.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.25e-04 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 2.25e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.27e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12625110.12795745 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 13809003.526953753 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12509514.611810673 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 4.95538 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 1.07892e-05 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 6300s, dt:6400s, Cycle: 6 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 1.05e-05 ) ; ( R ) = ( 1.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-04 ) ; ( Rwell ) = ( 1.43e-05 ) ; ( R ) = ( 5.53e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.33e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12829258.23115572 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 13963944.408440236 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12639439.309444282 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 5.17832 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 6.18038e-05 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 12700s, dt:12649.6s, Cycle: 7 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 1.43e-05 ) ; ( R ) = ( 3.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-01 ) ; ( Rwell ) = ( 1.97e-03 ) ; ( R ) = ( 1.48e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 1.07e-04 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 1.13e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.21e-02 ) ; ( Rwell ) = ( 6.93e-04 ) ; ( R ) = ( 8.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.60e-04 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 2.08e-04 ) ; ( R ) = ( 1.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.67e-05 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 1.44e-07 ) ; ( Rwell ) = ( 5.77e-09 ) ; ( R ) = ( 1.45e-07 ) ; + Last LinSolve(iter,res) = ( 5, 2.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13130771.101205045 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 14187170.187506337 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12740001.255915536 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 3.97889 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.131086 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 25349.6s, dt:7997.1s, Cycle: 8 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-02 ) ; ( Rwell ) = ( 2.33e-07 ) ; ( R ) = ( 6.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.66e-03 ) ; ( Rwell ) = ( 6.40e-04 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-04 ) ; ( Rwell ) = ( 1.60e-05 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13120649.79607198 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13936023.254895251 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12764351.084337302 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 1.37551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0699892 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 33346.7s, dt:7997.92s, Cycle: 9 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.60e-05 ) ; ( R ) = ( 6.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 2.72e-04 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 2.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.16e-04 ) ; ( Rwell ) = ( 1.49e-05 ) ; ( R ) = ( 2.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12969574.397761198 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 13606463.097934615 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 12612725.493361548 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.700345 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518183 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 41344.6s, dt:9672.86s, Cycle: 10 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.53e-05 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 9.42e-05 ) ; ( R ) = ( 6.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.36e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 2.51e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-03 ) ; ( Rwell ) = ( 1.50e-05 ) ; ( R ) = ( 2.12e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-05 ) ; ( Rwell ) = ( 1.62e-07 ) ; ( R ) = ( 2.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12809498.820794523 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 13351577.862489548 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 12359679.454863135 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.593641 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0841619 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 51017.5s, dt:8523.29s, Cycle: 11 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 4.14e-07 ) ; ( R ) = ( 6.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 2.03e-04 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.58e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 6.68e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.42e-03 ) ; ( Rwell ) = ( 1.37e-05 ) ; ( R ) = ( 1.42e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.00e-04 ) ; ( Rwell ) = ( 8.88e-08 ) ; ( R ) = ( 1.00e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.65e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12701900.118431661 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 13087242.032620579 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12208256.724149385 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.56181 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0676374 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 59540.8s, dt:8719.48s, Cycle: 12 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.54e-02 ) ; ( Rwell ) = ( 4.53e-07 ) ; ( R ) = ( 5.54e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.22e-04 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.83e-04 ) ; ( Rwell ) = ( 2.59e-06 ) ; ( R ) = ( 5.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12591012.737242643 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12863869.553929575 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12083953.433361951 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.169727 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599951 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 68260.3s, dt:9637.82s, Cycle: 13 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.59e-06 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 2.32e-05 ) ; ( R ) = ( 5.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12505240.031174501 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12695234.469816763 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 11989705.148871938 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.051335 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 77898.1s, dt:11721.4s, Cycle: 14 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.55e-06 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 2.04e-05 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.34e-03 ) ; ( Rwell ) = ( 8.22e-07 ) ; ( R ) = ( 1.34e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.01e-05 ) ; ( Rwell ) = ( 1.48e-08 ) ; ( R ) = ( 2.01e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12427105.46233864 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 12551990.88574718 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11892510.764417708 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218145 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0823281 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 89619.5s, dt:10489.8s, Cycle: 15 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.31e-02 ) ; ( Rwell ) = ( 1.90e-07 ) ; ( R ) = ( 6.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 1.52e-05 ) ; ( R ) = ( 5.35e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-04 ) ; ( Rwell ) = ( 6.98e-07 ) ; ( R ) = ( 5.74e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12391117.110042347 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12455893.400641864 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11844005.68368829 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.546342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629995 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 100109s, dt:11239.1s, Cycle: 16 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 6.98e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.29e-02 ) ; ( Rwell ) = ( 3.42e-05 ) ; ( R ) = ( 1.29e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-04 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 4.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12343238.498298468 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12380406.692840192 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11795370.089504316 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.373457 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0705466 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 111348s, dt:11180.9s, Cycle: 17 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.13e-02 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 6.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 2.95e-05 ) ; ( R ) = ( 2.81e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.65e-03 ) ; ( Rwell ) = ( 2.32e-06 ) ; ( R ) = ( 1.65e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.91e-07 ) ; ( Rwell ) = ( 3.19e-09 ) ; ( R ) = ( 5.91e-07 ) ; + Last LinSolve(iter,res) = ( 7, 1.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12305008.49662422 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12308717.064979061 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11728720.659626232 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.139568 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0529663 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 122529s, dt:13346s, Cycle: 18 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.80e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 5.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 5.92e-06 ) ; ( R ) = ( 5.92e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 2.96e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-02 ) ; ( Rwell ) = ( 5.49e-06 ) ; ( R ) = ( 2.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.15e-05 ) ; ( Rwell ) = ( 3.48e-07 ) ; ( R ) = ( 4.15e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12265776.179160925 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12266921.376007883 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 11664937.219629992 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.590758 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0567987 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 135875s, dt:15265.3s, Cycle: 19 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 3.20e-07 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 9.29e-06 ) ; ( R ) = ( 5.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.69e-02 ) ; ( Rwell ) = ( 4.49e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 3.55e-06 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.43e-04 ) ; ( Rwell ) = ( 3.91e-08 ) ; ( R ) = ( 1.43e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12247764.69903465 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12216892.619307533 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11626157.846513286 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367447 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0617914 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 151141s, dt:16559.9s, Cycle: 20 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 5.27e-08 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 1.18e-05 ) ; ( R ) = ( 6.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 2.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 5.91e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-02 ) ; ( Rwell ) = ( 8.50e-06 ) ; ( R ) = ( 2.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.10e-04 ) ; ( Rwell ) = ( 2.16e-07 ) ; ( R ) = ( 1.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12241424.274638133 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12172843.474961173 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11625140.911818217 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.614835 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0850177 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 167701s, dt:14487.7s, Cycle: 21 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 2.12e-07 ) ; ( R ) = ( 6.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.16e-05 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 3, 4.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-04 ) ; ( Rwell ) = ( 1.23e-06 ) ; ( R ) = ( 2.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12231373.493156876 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12142279.175079811 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 11607947.543207709 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.261335 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690862 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 182188s, dt:14614.9s, Cycle: 22 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 1.24e-06 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.41e-06 ) ; ( R ) = ( 3.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.98e-04 ) ; ( Rwell ) = ( 4.29e-07 ) ; ( R ) = ( 5.98e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12219903.256210728 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 12114155.967614925 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11580433.555529932 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.177384 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0502213 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 196803s, dt:18006.9s, Cycle: 23 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 4.37e-07 ) ; ( R ) = ( 5.41e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 8.61e-06 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.79e-02 ) ; ( Rwell ) = ( 4.20e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.70e-02 ) ; ( Rwell ) = ( 4.51e-06 ) ; ( R ) = ( 1.70e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.26e-05 ) ; ( Rwell ) = ( 9.52e-07 ) ; ( R ) = ( 8.26e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12206078.541398471 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12108016.295137031 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11563729.986555003 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.51044 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.086403 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 214810s, dt:15573.9s, Cycle: 24 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 9.52e-07 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 7.23e-06 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.21e-03 ) ; ( Rwell ) = ( 3.73e-06 ) ; ( R ) = ( 1.21e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-06 ) ; ( Rwell ) = ( 8.08e-09 ) ; ( R ) = ( 1.21e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.07e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12202292.69161467 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12098092.874529993 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11547879.809831511 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.317664 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728379 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 230384s, dt:15164.1s, Cycle: 25 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.38e-02 ) ; ( Rwell ) = ( 1.03e-08 ) ; ( R ) = ( 6.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-02 ) ; ( Rwell ) = ( 3.65e-05 ) ; ( R ) = ( 1.11e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.17e-05 ) ; ( Rwell ) = ( 8.43e-07 ) ; ( R ) = ( 5.17e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12205128.955945035 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12087612.902557736 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 11531547.12584477 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30265 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0522827 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 245548s, dt:18242.2s, Cycle: 26 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 8.43e-07 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.41e-02 ) ; ( Rwell ) = ( 8.55e-06 ) ; ( R ) = ( 5.41e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-03 ) ; ( Rwell ) = ( 1.81e-06 ) ; ( R ) = ( 1.87e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-06 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 1.26e-06 ) ; + Last LinSolve(iter,res) = ( 4, 1.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12201296.2884513 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 12086379.242075523 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11528273.290812435 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332354 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0570903 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 263790s, dt:20799.5s, Cycle: 27 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.35e-02 ) ; ( Rwell ) = ( 4.29e-08 ) ; ( R ) = ( 5.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 2.78e-05 ) ; ( R ) = ( 6.61e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 1.39e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 5.46e-06 ) ; ( R ) = ( 2.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.52e-04 ) ; ( Rwell ) = ( 5.82e-07 ) ; ( R ) = ( 7.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12201341.736672416 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12100237.91485237 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 11531489.76063267 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.40259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0806696 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 284590s, dt:18880.9s, Cycle: 28 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 5.82e-07 ) ; ( R ) = ( 6.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 8.56e-06 ) ; ( R ) = ( 4.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 2.44e-06 ) ; ( R ) = ( 4.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12208900.157226218 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12122409.263143126 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11539911.14137693 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.461503 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769527 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 303471s, dt:17708.3s, Cycle: 29 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 2.44e-06 ) ; ( R ) = ( 5.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.97e-02 ) ; ( Rwell ) = ( 1.70e-05 ) ; ( R ) = ( 4.97e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.59e-04 ) ; ( Rwell ) = ( 2.19e-06 ) ; ( R ) = ( 7.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12210358.904990789 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12139347.08609162 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11540272.33199013 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343024 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0538999 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 321179s, dt:20915.4s, Cycle: 30 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.40e-02 ) ; ( Rwell ) = ( 2.19e-06 ) ; ( R ) = ( 5.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.50e-02 ) ; ( Rwell ) = ( 1.27e-05 ) ; ( R ) = ( 6.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.82e-02 ) ; ( Rwell ) = ( 6.21e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.30e-03 ) ; ( Rwell ) = ( 1.83e-06 ) ; ( R ) = ( 4.30e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 3.50e-07 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12217207.370220903 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12152732.272274297 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 11543024.341771167 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.428054 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0717336 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 342095s, dt:20575.7s, Cycle: 31 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 3.50e-07 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 9.31e-06 ) ; ( R ) = ( 6.14e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.12e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 4.62e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.17e-03 ) ; ( Rwell ) = ( 1.08e-05 ) ; ( R ) = ( 8.17e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-05 ) ; ( Rwell ) = ( 1.30e-07 ) ; ( R ) = ( 1.21e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12219033.389914662 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 12172191.555568444 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11546799.080707248 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345441 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627033 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 362670s, dt:22112.3s, Cycle: 32 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.08e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 6.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 8.38e-06 ) ; ( R ) = ( 4.95e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.51e-03 ) ; ( Rwell ) = ( 1.65e-06 ) ; ( R ) = ( 2.51e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.20e-05 ) ; ( Rwell ) = ( 1.89e-07 ) ; ( R ) = ( 1.20e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12231075.514284937 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 12200679.493881637 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11551577.016415149 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.300057 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632143 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 384782s, dt:23640.1s, Cycle: 33 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.04e-06 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.20e-04 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 4.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12246814.64845288 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12238501.768077 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11567018.084864957 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.353251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624966 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 408423s, dt:25459.4s, Cycle: 34 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 5.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.77e-02 ) ; ( Rwell ) = ( 4.53e-06 ) ; ( R ) = ( 8.77e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 1.69e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.77e-03 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 8.77e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.70e-05 ) ; ( Rwell ) = ( 8.09e-07 ) ; ( R ) = ( 9.70e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12264627.596486025 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12281330.505631603 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11606435.201886138 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.764269 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0827001 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 433882s, dt:22712.3s, Cycle: 35 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 8.01e-07 ) ; ( R ) = ( 6.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.12e-02 ) ; ( Rwell ) = ( 5.31e-06 ) ; ( R ) = ( 6.12e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 7.56e-07 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.37e-06 ) ; ( Rwell ) = ( 2.72e-07 ) ; ( R ) = ( 6.37e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12275936.045081802 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12321955.5705242 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11630547.761646833 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.406801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637147 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 456594s, dt:24158.4s, Cycle: 36 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.78e-02 ) ; ( Rwell ) = ( 2.72e-07 ) ; ( R ) = ( 5.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 9.72e-06 ) ; ( R ) = ( 5.38e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.81e-03 ) ; ( Rwell ) = ( 6.89e-07 ) ; ( R ) = ( 7.81e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.39e-05 ) ; ( Rwell ) = ( 7.89e-08 ) ; ( R ) = ( 3.39e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.61e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12285313.535306845 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12361397.147042504 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 11651866.71159953 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.273299 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565795 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 480753s, dt:27698.7s, Cycle: 37 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.49e-02 ) ; ( Rwell ) = ( 7.89e-08 ) ; ( R ) = ( 5.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.51e-02 ) ; ( Rwell ) = ( 9.83e-06 ) ; ( R ) = ( 7.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.69e-02 ) ; ( Rwell ) = ( 4.87e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 5.95e-06 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.87e-05 ) ; ( Rwell ) = ( 1.86e-07 ) ; ( R ) = ( 3.87e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.04e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12297974.298119027 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12405781.778654108 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 11678346.378868548 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357965 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.100516 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 508451s, dt:21461.4s, Cycle: 38 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; ( R ) = ( 7.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 7.88e-06 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.70e-03 ) ; ( Rwell ) = ( 8.01e-07 ) ; ( R ) = ( 2.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.70e-06 ) ; ( Rwell ) = ( 6.66e-08 ) ; ( R ) = ( 1.70e-06 ) ; + Last LinSolve(iter,res) = ( 4, 1.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12316155.02447443 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 12440002.321245546 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 11702928.691955293 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.393111 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643637 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 529913s, dt:22678.8s, Cycle: 39 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.43e-02 ) ; ( Rwell ) = ( 7.35e-08 ) ; ( R ) = ( 5.43e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.31e-05 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.09e-03 ) ; ( Rwell ) = ( 1.94e-06 ) ; ( R ) = ( 6.09e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 6.33e-07 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 2, 9.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12328676.290304588 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12478128.635153437 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 11733526.090022296 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0528202 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 552592s, dt:27115.3s, Cycle: 40 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 6.39e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.42e-02 ) ; ( Rwell ) = ( 3.25e-05 ) ; ( R ) = ( 3.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-03 ) ; ( Rwell ) = ( 4.03e-06 ) ; ( R ) = ( 2.35e-03 ) ; + Last LinSolve(iter,res) = ( 3, 9.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-05 ) ; ( Rwell ) = ( 5.73e-08 ) ; ( R ) = ( 4.17e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12339220.143544266 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12518446.969444599 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 11766953.199131487 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367803 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0907127 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 579707s, dt:22647.7s, Cycle: 41 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.99e-02 ) ; ( Rwell ) = ( 6.46e-08 ) ; ( R ) = ( 6.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 2.26e-05 ) ; ( R ) = ( 6.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.91e-03 ) ; ( Rwell ) = ( 4.25e-07 ) ; ( R ) = ( 1.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.62e-06 ) ; ( Rwell ) = ( 2.68e-08 ) ; ( R ) = ( 3.62e-06 ) ; + Last LinSolve(iter,res) = ( 4, 1.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12347677.706137076 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 12550373.485692844 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11790626.608799871 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354671 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0604838 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 602355s, dt:24904.9s, Cycle: 42 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 3.31e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.20e-05 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.03e-03 ) ; ( Rwell ) = ( 2.03e-06 ) ; ( R ) = ( 1.03e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.04e-05 ) ; ( Rwell ) = ( 1.60e-08 ) ; ( R ) = ( 1.04e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12362834.044686304 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 12580977.320440948 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 11816220.953301053 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.357012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0783041 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 627260s, dt:23079.6s, Cycle: 43 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; ( R ) = ( 5.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 1.05e-05 ) ; ( R ) = ( 6.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.54e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 5.24e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.91e-03 ) ; ( Rwell ) = ( 8.63e-06 ) ; ( R ) = ( 2.91e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.76e-05 ) ; ( Rwell ) = ( 1.98e-07 ) ; ( R ) = ( 8.76e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12383731.208097566 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 12610695.582851695 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 11846585.118606668 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.477144 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0807947 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 650339s, dt:20928s, Cycle: 44 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.05e-07 ) ; ( R ) = ( 6.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.34e-02 ) ; ( Rwell ) = ( 7.83e-06 ) ; ( R ) = ( 2.34e-02 ) ; + Last LinSolve(iter,res) = ( 3, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.34e-04 ) ; ( Rwell ) = ( 8.85e-07 ) ; ( R ) = ( 2.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12398283.966298103 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12634435.886067819 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 11866612.316638183 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.170473 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561499 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 671267s, dt:24108s, Cycle: 45 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 8.76e-07 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.50e-02 ) ; ( Rwell ) = ( 1.22e-05 ) ; ( R ) = ( 8.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 6.34e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.97e-02 ) ; ( Rwell ) = ( 7.90e-06 ) ; ( R ) = ( 2.97e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.15e-04 ) ; ( Rwell ) = ( 2.63e-07 ) ; ( R ) = ( 2.15e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12414381.624079907 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12664703.27007813 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 11887352.638927791 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.391487 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0795173 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 695375s, dt:22104.5s, Cycle: 46 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.69e-07 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 9.96e-06 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.28e-06 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.70e-07 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 5.70e-07 ) ; + Last LinSolve(iter,res) = ( 5, 4.38e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12432387.694280216 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12688609.363371547 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 11908261.858793287 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.276707 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606353 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 717480s, dt:24269s, Cycle: 47 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.46e-02 ) ; ( Rwell ) = ( 2.22e-08 ) ; ( R ) = ( 5.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.74e-02 ) ; ( Rwell ) = ( 1.26e-05 ) ; ( R ) = ( 5.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.69e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.93e-02 ) ; ( Rwell ) = ( 6.32e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.07e-02 ) ; ( Rwell ) = ( 6.31e-06 ) ; ( R ) = ( 1.07e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 2.52e-07 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12451499.604383184 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12714730.048355343 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 11929378.973770352 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.361726 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728298 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 741749s, dt:23632.1s, Cycle: 48 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 2.57e-07 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.49e-02 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 7.49e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 5.01e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.70e-03 ) ; ( Rwell ) = ( 4.83e-06 ) ; ( R ) = ( 9.70e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.92e-05 ) ; ( Rwell ) = ( 1.23e-07 ) ; ( R ) = ( 3.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12470411.467630122 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12742731.437458526 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 11956802.943074843 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.626978 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0669106 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 765381s, dt:24348.5s, Cycle: 49 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 9.38e-06 ) ; ( R ) = ( 4.06e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.65e-04 ) ; ( Rwell ) = ( 7.64e-07 ) ; ( R ) = ( 2.65e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12490127.422193186 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12770864.286273163 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 11979754.244079541 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.293943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688207 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 789729s, dt:24625.1s, Cycle: 50 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 7.70e-07 ) ; ( R ) = ( 6.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.50e-02 ) ; ( Rwell ) = ( 1.11e-05 ) ; ( R ) = ( 1.50e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-03 ) ; ( Rwell ) = ( 3.42e-07 ) ; ( R ) = ( 1.76e-03 ) ; + Last LinSolve(iter,res) = ( 4, 5.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.56e-06 ) ; ( Rwell ) = ( 6.99e-08 ) ; ( R ) = ( 1.56e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12509134.461597566 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12794861.492555017 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 11998267.032977767 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.267228 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0599686 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 814354s, dt:27226.2s, Cycle: 51 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 6.70e-08 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 1.70e-05 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.33e-04 ) ; ( Rwell ) = ( 8.28e-07 ) ; ( R ) = ( 5.33e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12529614.621992538 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 12817620.313759927 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12016979.693896176 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.365322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769607 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 841581s, dt:25533.5s, Cycle: 52 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 8.34e-07 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 1.35e-05 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.72e-03 ) ; ( Rwell ) = ( 6.83e-07 ) ; ( R ) = ( 2.72e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.35e-06 ) ; ( Rwell ) = ( 5.13e-08 ) ; ( R ) = ( 2.35e-06 ) ; + Last LinSolve(iter,res) = ( 3, 2.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12549971.184365254 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 12838144.192098387 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 12037074.4552305 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0518598 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 867114s, dt:30866s, Cycle: 53 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.34e-02 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 5.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.19e-02 ) ; ( Rwell ) = ( 1.15e-05 ) ; ( R ) = ( 7.19e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.98e-02 ) ; ( Rwell ) = ( 5.74e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 6.36e-06 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-04 ) ; ( Rwell ) = ( 9.77e-07 ) ; ( R ) = ( 2.94e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12573403.64955174 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 12868769.289469818 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12069161.634467982 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.647297 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640486 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 897980s, dt:32720.6s, Cycle: 54 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.79e-02 ) ; ( Rwell ) = ( 9.80e-07 ) ; ( R ) = ( 5.79e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.00e-05 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.58e-03 ) ; ( Rwell ) = ( 8.19e-07 ) ; ( R ) = ( 2.58e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.38e-06 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 2.38e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12598123.730083294 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 12900655.619589217 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12097720.108980944 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.397388 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0943531 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 930701s, dt:26560.3s, Cycle: 55 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 6.59e-08 ) ; ( R ) = ( 7.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 2.95e-05 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.29e-03 ) ; ( Rwell ) = ( 2.09e-07 ) ; ( R ) = ( 1.29e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.36e-07 ) ; ( Rwell ) = ( 9.94e-09 ) ; ( R ) = ( 6.36e-07 ) ; + Last LinSolve(iter,res) = ( 5, 5.37e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12621977.489585243 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 12925620.49873713 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12119152.52720531 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.398825 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0716018 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 957261s, dt:26161.2s, Cycle: 56 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.07e-02 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 7.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.03e-02 ) ; ( Rwell ) = ( 1.92e-05 ) ; ( R ) = ( 2.03e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 8.52e-07 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.44e-07 ) ; ( Rwell ) = ( 7.34e-09 ) ; ( R ) = ( 8.44e-07 ) ; + Last LinSolve(iter,res) = ( 5, 2.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12641294.968619782 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 12947112.826718764 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12136411.107143389 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.193761 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0590968 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 983422s, dt:29192.6s, Cycle: 57 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.03e-02 ) ; ( Rwell ) = ( 1.22e-08 ) ; ( R ) = ( 7.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.71e-02 ) ; ( Rwell ) = ( 1.25e-05 ) ; ( R ) = ( 2.71e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.82e-03 ) ; ( Rwell ) = ( 5.85e-07 ) ; ( R ) = ( 2.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-05 ) ; ( Rwell ) = ( 5.56e-08 ) ; ( R ) = ( 1.06e-05 ) ; + Last LinSolve(iter,res) = ( 2, 6.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12661267.84399922 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 12969502.358913276 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12156066.849880021 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.368153 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0802112 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.01261e+06s, dt:26605.2s, Cycle: 58 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.39e-02 ) ; ( Rwell ) = ( 5.95e-08 ) ; ( R ) = ( 6.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 1.38e-05 ) ; ( R ) = ( 4.53e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.57e-04 ) ; ( Rwell ) = ( 7.38e-07 ) ; ( R ) = ( 4.57e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12679452.46134544 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 12989572.12966096 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12175042.022970038 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.297116 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686522 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03922e+06s, dt:26951.2s, Cycle: 59 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 7.41e-07 ) ; ( R ) = ( 6.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 1.17e-05 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.56e-04 ) ; ( Rwell ) = ( 5.95e-07 ) ; ( R ) = ( 5.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12701498.607656274 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 13011245.151056368 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12196944.605860006 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.33519 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0610078 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.06617e+06s, dt:29475.5s, Cycle: 60 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.35e-02 ) ; ( Rwell ) = ( 5.98e-07 ) ; ( R ) = ( 6.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.16e-02 ) ; ( Rwell ) = ( 1.74e-05 ) ; ( R ) = ( 7.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.08e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.46e-02 ) ; ( Rwell ) = ( 8.62e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.02e-05 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.73e-05 ) ; ( Rwell ) = ( 5.45e-07 ) ; ( R ) = ( 4.73e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12732558.981495058 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 13036804.937833631 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12227017.36245946 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.467828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728617 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.09565e+06s, dt:28693.5s, Cycle: 61 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 5.37e-07 ) ; ( R ) = ( 6.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.33e-02 ) ; ( Rwell ) = ( 1.64e-05 ) ; ( R ) = ( 5.33e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.07e-04 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 6.07e-04 ) ; + Last LinSolve(iter,res) = ( 5, 2.90e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12760178.762729296 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13061610.719050955 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12256241.954657773 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.408467 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0714306 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.12434e+06s, dt:28307.8s, Cycle: 62 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 2.32e-08 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.80e-02 ) ; ( Rwell ) = ( 1.35e-05 ) ; ( R ) = ( 2.80e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.25e-04 ) ; ( Rwell ) = ( 6.30e-07 ) ; ( R ) = ( 5.25e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12783977.547966564 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13085737.172500346 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12282394.005817333 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332545 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632688 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.15265e+06s, dt:30246.8s, Cycle: 63 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 6.33e-07 ) ; ( R ) = ( 6.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 9.26e-06 ) ; ( R ) = ( 6.95e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.20e-02 ) ; ( Rwell ) = ( 4.95e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.44e-03 ) ; ( Rwell ) = ( 1.15e-05 ) ; ( R ) = ( 7.44e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.97e-05 ) ; ( Rwell ) = ( 5.72e-07 ) ; ( R ) = ( 5.97e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12808026.528146418 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13111720.07572803 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12310253.398490662 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.430615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0613937 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18289e+06s, dt:32947.3s, Cycle: 64 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.25e-02 ) ; ( Rwell ) = ( 5.65e-07 ) ; ( R ) = ( 6.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.02e-02 ) ; ( Rwell ) = ( 7.60e-06 ) ; ( R ) = ( 2.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12834408.551860178 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13138789.33626655 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12336562.239663858 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.300551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0723245 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.21584e+06s, dt:32233.7s, Cycle: 65 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 6.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.45e-02 ) ; ( Rwell ) = ( 1.98e-05 ) ; ( R ) = ( 3.45e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-03 ) ; ( Rwell ) = ( 6.79e-07 ) ; ( R ) = ( 2.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-06 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 1.88e-06 ) ; + Last LinSolve(iter,res) = ( 3, 2.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12857394.946645504 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 13163981.346056897 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12359309.219390113 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.211322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.059703 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.24808e+06s, dt:35738.5s, Cycle: 66 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 6.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-02 ) ; ( Rwell ) = ( 2.18e-05 ) ; ( R ) = ( 6.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.11e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 1.09e-05 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 2.58e-06 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12887374.948878696 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13195159.656043798 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12391185.169738056 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.374445 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0717555 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.28381e+06s, dt:35150.8s, Cycle: 67 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.23e-02 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.15e-02 ) ; ( Rwell ) = ( 2.81e-05 ) ; ( R ) = ( 2.15e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.26e-04 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 3.26e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12918513.639511287 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13224581.746866737 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12424443.123457063 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0760672 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.31896e+06s, dt:33230.6s, Cycle: 68 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 6.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.72e-05 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 3.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 7.87e-07 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.11e-06 ) ; ( Rwell ) = ( 1.60e-07 ) ; ( R ) = ( 4.11e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12944100.778878445 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13252254.903222507 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12453020.390070518 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.366791 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641019 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.3522e+06s, dt:35208.4s, Cycle: 69 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.89e-02 ) ; ( Rwell ) = ( 1.54e-07 ) ; ( R ) = ( 5.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.20e-05 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 6.36e-07 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.55e-07 ) ; ( Rwell ) = ( 7.07e-09 ) ; ( R ) = ( 6.55e-07 ) ; + Last LinSolve(iter,res) = ( 5, 6.45e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 12970191.047815965 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13281802.700572215 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 12483498.779057475 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.413274 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0733872 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.3874e+06s, dt:34108.1s, Cycle: 70 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 1.20e-08 ) ; ( R ) = ( 6.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 2.34e-05 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-03 ) ; ( Rwell ) = ( 9.16e-07 ) ; ( R ) = ( 1.55e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.16e-06 ) ; ( Rwell ) = ( 5.76e-08 ) ; ( R ) = ( 2.16e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12998427.934969736 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 13309669.222884776 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 12513992.97195591 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.351184 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722513 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.42151e+06s, dt:33392.1s, Cycle: 71 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.97e-02 ) ; ( Rwell ) = ( 6.27e-08 ) ; ( R ) = ( 6.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.44e-02 ) ; ( Rwell ) = ( 1.06e-05 ) ; ( R ) = ( 3.44e-02 ) ; + Last LinSolve(iter,res) = ( 3, 6.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.39e-03 ) ; ( Rwell ) = ( 1.24e-07 ) ; ( R ) = ( 1.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 2.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.79e-05 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 1.79e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13027627.05407019 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13338000.183257852 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 12543330.516170574 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313628 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649917 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4549e+06s, dt:35064.6s, Cycle: 72 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 7.17e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 7.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.23e-02 ) ; ( Rwell ) = ( 1.66e-05 ) ; ( R ) = ( 3.23e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.84e-04 ) ; ( Rwell ) = ( 1.34e-06 ) ; ( R ) = ( 7.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13060155.325777616 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13368628.336166209 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 12574892.387566976 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35213 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0645253 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.48997e+06s, dt:36993.5s, Cycle: 73 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.64e-02 ) ; ( Rwell ) = ( 1.34e-06 ) ; ( R ) = ( 6.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 1.47e-05 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.72e-04 ) ; ( Rwell ) = ( 4.43e-07 ) ; ( R ) = ( 1.72e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13092153.632866511 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13400491.547501344 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12606991.971356643 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278018 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0516321 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.52696e+06s, dt:44836.9s, Cycle: 74 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.56e-02 ) ; ( Rwell ) = ( 4.47e-07 ) ; ( R ) = ( 6.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 1.56e-05 ) ; ( R ) = ( 6.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.38e-03 ) ; ( Rwell ) = ( 9.35e-07 ) ; ( R ) = ( 6.38e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-05 ) ; ( Rwell ) = ( 8.68e-08 ) ; ( R ) = ( 5.16e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13129619.197478218 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13437741.139278509 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 12645349.36462271 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.384769 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0912752 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.5718e+06s, dt:37282.7s, Cycle: 75 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 9.14e-08 ) ; ( R ) = ( 6.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.13e-02 ) ; ( Rwell ) = ( 1.12e-05 ) ; ( R ) = ( 7.13e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.30e-02 ) ; ( Rwell ) = ( 5.64e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-02 ) ; ( Rwell ) = ( 1.32e-05 ) ; ( R ) = ( 1.25e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.21e-04 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 1.21e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13160440.127342993 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 13469981.146705272 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 12678579.214447862 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.430766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0801911 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.60908e+06s, dt:33984.3s, Cycle: 76 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.09e-02 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 6.09e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.49e-02 ) ; ( Rwell ) = ( 1.99e-05 ) ; ( R ) = ( 3.49e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.23e-03 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 5.23e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.60e-05 ) ; ( Rwell ) = ( 2.96e-08 ) ; ( R ) = ( 1.60e-05 ) ; + Last LinSolve(iter,res) = ( 4, 2.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13187762.131398693 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13499754.292856757 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 12708778.778199863 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696726 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.64307e+06s, dt:34090.6s, Cycle: 77 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 2.43e-08 ) ; ( R ) = ( 6.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 1.01e-05 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.47e-04 ) ; ( Rwell ) = ( 3.96e-07 ) ; ( R ) = ( 8.47e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13215869.855355034 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13528218.183994727 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 12738946.094332887 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.331686 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0606139 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.67716e+06s, dt:37437.1s, Cycle: 78 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 3.99e-07 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.16e-05 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.31e-04 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 4.31e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13246728.586013984 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 13558790.299118744 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12770061.160242913 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.376986 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0906444 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.71459e+06s, dt:31285.9s, Cycle: 79 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 1.10e-05 ) ; ( R ) = ( 5.37e-02 ) ; + Last LinSolve(iter,res) = ( 3, 7.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.80e-04 ) ; ( Rwell ) = ( 3.95e-07 ) ; ( R ) = ( 4.80e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13272735.992848968 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13585942.471840788 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 12796836.299479937 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369233 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578417 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.74588e+06s, dt:35383s, Cycle: 80 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 3.98e-07 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 1.46e-05 ) ; ( R ) = ( 2.83e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-04 ) ; ( Rwell ) = ( 7.18e-07 ) ; ( R ) = ( 1.64e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13300823.677502599 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13616453.598649742 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 12826230.171938997 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294212 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624271 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.78126e+06s, dt:38133.2s, Cycle: 81 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 7.11e-07 ) ; ( R ) = ( 6.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.81e-02 ) ; ( Rwell ) = ( 1.60e-05 ) ; ( R ) = ( 5.81e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.18e-03 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 5.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.18e-05 ) ; ( Rwell ) = ( 1.38e-07 ) ; ( R ) = ( 1.18e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.67e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13331836.623200728 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13648476.467122825 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 12858956.476494333 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.376962 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642484 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8194e+06s, dt:40343.1s, Cycle: 82 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.66e-02 ) ; ( Rwell ) = ( 1.52e-05 ) ; ( R ) = ( 3.66e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 2.21e-06 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.40e-05 ) ; ( Rwell ) = ( 3.34e-08 ) ; ( R ) = ( 4.40e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13366539.404852029 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270262836 sm3/s +wellControls2: BHP (at the specified reference elevation): 13681035.10826914 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270262586 sm3/s +wellControls3: BHP (at the specified reference elevation): 12893688.218312168 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.316823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691823 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.85974e+06s, dt:40659.8s, Cycle: 83 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.85e-08 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.26e-02 ) ; ( Rwell ) = ( 7.20e-06 ) ; ( R ) = ( 3.26e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.95e-04 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 7.95e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13400691.87729028 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 13714067.563133286 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 12928157.630033297 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320793 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0554493 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9004e+06s, dt:47200.8s, Cycle: 84 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.95e-02 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 6.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.00e-02 ) ; ( Rwell ) = ( 1.45e-05 ) ; ( R ) = ( 5.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.68e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-03 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 2.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-05 ) ; ( Rwell ) = ( 3.17e-08 ) ; ( R ) = ( 3.49e-05 ) ; + Last LinSolve(iter,res) = ( 5, 1.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13441315.950165523 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13754149.413672918 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 12969596.094050923 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.49619 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0930372 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.9476e+06s, dt:38708.1s, Cycle: 85 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.59e-02 ) ; ( Rwell ) = ( 2.65e-08 ) ; ( R ) = ( 6.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.01e-02 ) ; ( Rwell ) = ( 6.78e-06 ) ; ( R ) = ( 3.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.89e-03 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 1.89e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.35e-05 ) ; ( Rwell ) = ( 4.59e-08 ) ; ( R ) = ( 3.35e-05 ) ; + Last LinSolve(iter,res) = ( 5, 2.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13474419.128230102 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 13785942.249278821 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 13004701.85062461 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.356482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774588 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.98631e+06s, dt:36140.8s, Cycle: 86 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 7.08e-06 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.58e-04 ) ; ( Rwell ) = ( 8.11e-07 ) ; ( R ) = ( 7.58e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13502612.376966357 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13814994.403738586 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13035573.786488155 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.333766 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671496 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.02245e+06s, dt:37149.3s, Cycle: 87 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.78e-02 ) ; ( Rwell ) = ( 8.13e-07 ) ; ( R ) = ( 6.78e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.79e-02 ) ; ( Rwell ) = ( 8.30e-06 ) ; ( R ) = ( 3.79e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-04 ) ; ( Rwell ) = ( 4.49e-07 ) ; ( R ) = ( 3.21e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13531580.408481648 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13844968.101507554 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13066622.307165695 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.354124 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612134 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.0596e+06s, dt:40542s, Cycle: 88 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.96e-02 ) ; ( Rwell ) = ( 4.49e-07 ) ; ( R ) = ( 6.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 7.31e-06 ) ; ( R ) = ( 4.51e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.04e-03 ) ; ( Rwell ) = ( 5.72e-07 ) ; ( R ) = ( 5.04e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 5.22e-08 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13565268.29922534 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13881964.847294748 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13101433.346034376 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.502896 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0791822 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.10014e+06s, dt:37281.7s, Cycle: 89 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 5.68e-08 ) ; ( R ) = ( 6.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 6.97e-06 ) ; ( R ) = ( 3.94e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-04 ) ; ( Rwell ) = ( 6.23e-07 ) ; ( R ) = ( 3.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13596290.597189061 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 13914754.97479742 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 13133311.989444464 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.301921 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0735307 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.13742e+06s, dt:36068.9s, Cycle: 90 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 6.26e-07 ) ; ( R ) = ( 6.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 9.77e-06 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-04 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 4.54e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13624671.70933674 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 13943863.810217032 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 13162005.299108393 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234282 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0629464 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17349e+06s, dt:38666.4s, Cycle: 91 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 6.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 1.23e-05 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 3, 8.80e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13653481.825449372 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 13973462.57340018 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls3: BHP (at the specified reference elevation): 13191319.746792123 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.231963 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0544964 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.21216e+06s, dt:45364.6s, Cycle: 92 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 6.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-01 ) ; ( Rwell ) = ( 6.54e-06 ) ; ( R ) = ( 1.14e-01 ) ; + Last LinSolve(iter,res) = ( 4, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 3.26e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 5.77e-06 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.41e-03 ) ; ( Rwell ) = ( 9.85e-07 ) ; ( R ) = ( 1.41e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.12e-06 ) ; ( Rwell ) = ( 1.26e-08 ) ; ( R ) = ( 2.12e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13687410.066707676 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14008230.158798555 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 13225224.649853665 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.423195 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0766927 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.25752e+06s, dt:42646.4s, Cycle: 93 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.01e-02 ) ; ( Rwell ) = ( 1.67e-08 ) ; ( R ) = ( 6.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.88e-02 ) ; ( Rwell ) = ( 1.27e-05 ) ; ( R ) = ( 5.88e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.69e-03 ) ; ( Rwell ) = ( 7.82e-07 ) ; ( R ) = ( 2.69e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.42e-06 ) ; ( Rwell ) = ( 4.85e-08 ) ; ( R ) = ( 6.42e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13718945.919587607 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 14039717.448796796 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13257515.934802111 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274041 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0747813 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.30017e+06s, dt:40789s, Cycle: 94 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 5.25e-08 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 9.42e-06 ) ; ( R ) = ( 3.65e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.89e-04 ) ; ( Rwell ) = ( 3.28e-07 ) ; ( R ) = ( 3.89e-04 ) ; + Last LinSolve(iter,res) = ( 6, 8.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13750346.67507955 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14070797.652581695 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 13290371.604571948 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683097 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.34096e+06s, dt:41456.3s, Cycle: 95 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 6.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.53e-02 ) ; ( Rwell ) = ( 8.15e-06 ) ; ( R ) = ( 2.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.94e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-04 ) ; ( Rwell ) = ( 4.82e-07 ) ; ( R ) = ( 3.58e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13783026.73442358 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14104442.4227627 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13324889.902691344 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337444 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0640235 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.38241e+06s, dt:43958.4s, Cycle: 96 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.77e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 6.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.18e-02 ) ; ( Rwell ) = ( 1.31e-05 ) ; ( R ) = ( 8.18e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.71e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 6.34e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.57e-03 ) ; ( Rwell ) = ( 2.54e-06 ) ; ( R ) = ( 5.57e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.57e-05 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 2.57e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13820324.246797236 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14140083.155959506 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13363755.165600538 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.434593 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0854026 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.42637e+06s, dt:38335s, Cycle: 97 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 1.69e-07 ) ; ( R ) = ( 6.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 8.31e-06 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.21e-05 ) ; ( Rwell ) = ( 9.64e-07 ) ; ( R ) = ( 7.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13851765.050729394 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 14171151.32454203 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 13396191.236308977 Pa +wellControls3: Total rate: 56.328373541922936 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026309 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.245942 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.081693 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.46471e+06s, dt:34493.7s, Cycle: 98 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.58e-02 ) ; ( Rwell ) = ( 9.66e-07 ) ; ( R ) = ( 6.58e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.47e-02 ) ; ( Rwell ) = ( 8.27e-06 ) ; ( R ) = ( 5.47e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-02 ) ; ( Rwell ) = ( 1.66e-07 ) ; ( R ) = ( 1.79e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.26e-03 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 1.26e-03 ) ; + Last LinSolve(iter,res) = ( 3, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 5.76e-07 ) ; ( Rwell ) = ( 1.04e-09 ) ; ( R ) = ( 5.76e-07 ) ; + Last LinSolve(iter,res) = ( 6, 3.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13880127.634812612 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 14199481.407176144 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13426057.327555688 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343704 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601568 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.4992e+06s, dt:38061.8s, Cycle: 99 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.27e-02 ) ; ( Rwell ) = ( 1.07e-08 ) ; ( R ) = ( 6.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 6.24e-06 ) ; ( R ) = ( 1.01e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.54e-05 ) ; ( Rwell ) = ( 4.20e-07 ) ; ( R ) = ( 8.54e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13910737.746928826 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14230934.207834318 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13458208.885140136 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369396 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721771 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.53726e+06s, dt:37288.7s, Cycle: 100 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.94e-02 ) ; ( Rwell ) = ( 4.14e-07 ) ; ( R ) = ( 5.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.09e-02 ) ; ( Rwell ) = ( 1.07e-05 ) ; ( R ) = ( 2.09e-02 ) ; + Last LinSolve(iter,res) = ( 3, 9.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.41e-04 ) ; ( Rwell ) = ( 4.25e-07 ) ; ( R ) = ( 2.41e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13940297.14323035 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 14260953.926224355 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13488363.249477644 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.238837 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0624833 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.57455e+06s, dt:40163.9s, Cycle: 101 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 4.19e-07 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.58e-02 ) ; ( Rwell ) = ( 6.95e-06 ) ; ( R ) = ( 1.58e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.61e-05 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 5.61e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 13971981.904788157 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14292136.034366312 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 13520164.94751824 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.350823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.061257 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.61471e+06s, dt:43812s, Cycle: 102 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 5.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 4.75e-06 ) ; ( R ) = ( 4.56e-02 ) ; + Last LinSolve(iter,res) = ( 4, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-04 ) ; ( Rwell ) = ( 3.34e-07 ) ; ( R ) = ( 3.63e-04 ) ; + Last LinSolve(iter,res) = ( 6, 9.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14006066.985692771 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 14326312.13152389 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 13554873.3469955 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341485 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0642636 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.65853e+06s, dt:46343.8s, Cycle: 103 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.92e-02 ) ; ( Rwell ) = ( 3.28e-07 ) ; ( R ) = ( 5.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.14e-02 ) ; ( Rwell ) = ( 6.88e-06 ) ; ( R ) = ( 6.14e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.02e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 3.60e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.00e-02 ) ; ( Rwell ) = ( 3.56e-06 ) ; ( R ) = ( 2.00e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.65e-05 ) ; ( Rwell ) = ( 6.52e-08 ) ; ( R ) = ( 4.65e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14042293.195181489 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 14362837.031730963 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 13592279.624629235 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341843 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0573694 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.70487e+06s, dt:52680.9s, Cycle: 104 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.96e-02 ) ; ( Rwell ) = ( 6.52e-08 ) ; ( R ) = ( 5.96e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.63e-02 ) ; ( Rwell ) = ( 6.02e-06 ) ; ( R ) = ( 5.63e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.57e-03 ) ; ( Rwell ) = ( 8.78e-08 ) ; ( R ) = ( 3.57e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.84e-06 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 9.84e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14083946.335352253 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 14405470.85919018 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 13636735.539005922 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.40901 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0864538 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.75755e+06s, dt:45544s, Cycle: 105 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.48e-02 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 6.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 6.83e-06 ) ; ( R ) = ( 4.89e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.55e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.59e-04 ) ; ( Rwell ) = ( 1.68e-06 ) ; ( R ) = ( 2.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.28e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14120639.440438483 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 14442633.964747258 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 13676859.973162431 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337407 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0752179 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.8031e+06s, dt:43387.9s, Cycle: 106 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 6.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.64e-02 ) ; ( Rwell ) = ( 7.35e-06 ) ; ( R ) = ( 1.64e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.71e-04 ) ; ( Rwell ) = ( 7.23e-07 ) ; ( R ) = ( 2.71e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14155179.006579157 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14477868.857211178 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 13712906.491734624 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.289773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0680674 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.84648e+06s, dt:44201.4s, Cycle: 107 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 7.15e-07 ) ; ( R ) = ( 6.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 3.72e-06 ) ; ( R ) = ( 3.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.62e-04 ) ; ( Rwell ) = ( 8.94e-08 ) ; ( R ) = ( 4.62e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14190952.970535275 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 14513687.458788354 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 13750327.485665461 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.287681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0698275 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.89068e+06s, dt:44274.2s, Cycle: 108 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.49e-02 ) ; ( Rwell ) = ( 8.45e-08 ) ; ( R ) = ( 6.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 3.85e-06 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-04 ) ; ( Rwell ) = ( 9.31e-07 ) ; ( R ) = ( 1.79e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14226437.209085902 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14548797.077120516 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13786950.735190177 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.283262 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691958 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.93496e+06s, dt:44615.8s, Cycle: 109 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 9.32e-07 ) ; ( R ) = ( 6.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.36e-02 ) ; ( Rwell ) = ( 2.46e-06 ) ; ( R ) = ( 1.36e-02 ) ; + Last LinSolve(iter,res) = ( 7, 2.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.47e-03 ) ; ( Rwell ) = ( 5.87e-07 ) ; ( R ) = ( 3.47e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.20e-05 ) ; ( Rwell ) = ( 1.92e-07 ) ; ( R ) = ( 3.20e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14260963.120797087 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 14584087.261414997 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 13822878.050468406 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639257 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.97957e+06s, dt:47355.4s, Cycle: 110 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.29e-02 ) ; ( Rwell ) = ( 1.95e-07 ) ; ( R ) = ( 6.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.85e-02 ) ; ( Rwell ) = ( 6.11e-06 ) ; ( R ) = ( 1.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 5.58e-07 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14295870.418138325 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14619991.87866204 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 13859118.42962807 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.319821 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065899 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.02693e+06s, dt:49280.2s, Cycle: 111 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 5.51e-07 ) ; ( R ) = ( 5.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.41e-02 ) ; ( Rwell ) = ( 4.87e-06 ) ; ( R ) = ( 4.41e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.50e-03 ) ; ( Rwell ) = ( 8.85e-07 ) ; ( R ) = ( 4.50e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.32e-05 ) ; ( Rwell ) = ( 9.86e-08 ) ; ( R ) = ( 1.32e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14333043.506749043 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 14656277.412526961 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13896739.776498884 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.319943 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607209 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.07621e+06s, dt:54057.3s, Cycle: 112 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.98e-02 ) ; ( Rwell ) = ( 9.42e-08 ) ; ( R ) = ( 5.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.88e-02 ) ; ( Rwell ) = ( 3.56e-06 ) ; ( R ) = ( 4.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 7, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.84e-05 ) ; ( Rwell ) = ( 5.55e-07 ) ; ( R ) = ( 9.84e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14374403.93533906 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 14697095.253927981 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 13939283.166725334 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.328685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626019 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.13027e+06s, dt:58154.8s, Cycle: 113 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.85e-02 ) ; ( Rwell ) = ( 5.49e-07 ) ; ( R ) = ( 5.85e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.38e-05 ) ; ( R ) = ( 4.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-03 ) ; ( Rwell ) = ( 9.22e-07 ) ; ( R ) = ( 1.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.79e-05 ) ; ( Rwell ) = ( 1.83e-09 ) ; ( R ) = ( 7.79e-05 ) ; + Last LinSolve(iter,res) = ( 7, 1.13e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14419031.453978155 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 14741659.959523382 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 13985005.362046823 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.352001 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0735571 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.18842e+06s, dt:56249.2s, Cycle: 114 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.22e-02 ) ; ( Rwell ) = ( 9.38e-09 ) ; ( R ) = ( 6.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 9.33e-06 ) ; ( R ) = ( 3.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.31e-02 ) ; ( Rwell ) = ( 2.80e-07 ) ; ( R ) = ( 1.31e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.44e-05 ) ; ( Rwell ) = ( 1.46e-07 ) ; ( R ) = ( 5.44e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14461038.094725853 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 14785942.903685559 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 14028286.177444214 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.34241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658974 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.24467e+06s, dt:58536.4s, Cycle: 115 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.68e-02 ) ; ( Rwell ) = ( 1.41e-07 ) ; ( R ) = ( 6.68e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 4.72e-06 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.57e-03 ) ; ( Rwell ) = ( 7.79e-08 ) ; ( R ) = ( 1.57e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.36e-05 ) ; ( Rwell ) = ( 4.60e-08 ) ; ( R ) = ( 1.36e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14503483.181743532 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 14830221.449630735 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 14071845.574096119 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335682 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0649749 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.30321e+06s, dt:61478.6s, Cycle: 116 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.80e-02 ) ; ( Rwell ) = ( 4.97e-08 ) ; ( R ) = ( 6.80e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.51e-02 ) ; ( Rwell ) = ( 9.31e-06 ) ; ( R ) = ( 2.51e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-04 ) ; ( Rwell ) = ( 3.09e-07 ) ; ( R ) = ( 3.31e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14546461.43017271 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14874222.418943292 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 14115903.419889962 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.315953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0648772 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.36469e+06s, dt:64631.9s, Cycle: 117 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.93e-02 ) ; ( Rwell ) = ( 3.11e-07 ) ; ( R ) = ( 6.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.16e-06 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.19e-02 ) ; ( Rwell ) = ( 3.32e-06 ) ; ( R ) = ( 1.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.20e-05 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 4.20e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14592280.60914108 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 14920148.438775413 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14163396.169631716 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.372901 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0770153 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.42932e+06s, dt:60584.2s, Cycle: 118 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.90e-02 ) ; ( Rwell ) = ( 3.09e-07 ) ; ( R ) = ( 5.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 4.77e-06 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-04 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 2.03e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14635593.515542844 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 14962553.76666945 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 14208351.683413707 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313846 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665987 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.4899e+06s, dt:62612.4s, Cycle: 119 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.93e-02 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 5.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.86e-02 ) ; ( Rwell ) = ( 3.55e-06 ) ; ( R ) = ( 6.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 1.96e-06 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.85e-05 ) ; ( Rwell ) = ( 2.16e-07 ) ; ( R ) = ( 5.85e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.98e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14679775.366461203 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15007953.416913796 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 14254613.718854988 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.382627 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0706419 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.55252e+06s, dt:62231.9s, Cycle: 120 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 2.11e-07 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.29e-02 ) ; ( Rwell ) = ( 2.68e-06 ) ; ( R ) = ( 5.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.24e-03 ) ; ( Rwell ) = ( 3.32e-06 ) ; ( R ) = ( 8.24e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-04 ) ; ( Rwell ) = ( 4.97e-07 ) ; ( R ) = ( 1.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14724901.524871955 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 15053316.86818153 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls3: BHP (at the specified reference elevation): 14301877.94020407 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.340615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0765534 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.61475e+06s, dt:58576s, Cycle: 121 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.04e-02 ) ; ( Rwell ) = ( 4.98e-07 ) ; ( R ) = ( 6.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.17e-02 ) ; ( Rwell ) = ( 7.33e-06 ) ; ( R ) = ( 6.17e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.53e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.95e-02 ) ; ( Rwell ) = ( 3.65e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.76e-03 ) ; ( Rwell ) = ( 1.90e-06 ) ; ( R ) = ( 2.76e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.29e-05 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 2.29e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14767513.046303907 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 15095384.212229079 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 14347334.781352207 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.358849 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0745105 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.67332e+06s, dt:56163.4s, Cycle: 122 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.36e-02 ) ; ( Rwell ) = ( 5.37e-08 ) ; ( R ) = ( 6.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.10e-04 ) ; ( Rwell ) = ( 2.53e-07 ) ; ( R ) = ( 2.10e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14806896.593973778 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15134798.257134553 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 14388226.318145651 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.267376 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687868 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.72949e+06s, dt:56819.9s, Cycle: 123 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.57e-02 ) ; ( Rwell ) = ( 2.48e-07 ) ; ( R ) = ( 6.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 5.30e-06 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.43e-05 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 7.43e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14845497.162660463 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15174371.424139135 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 14428271.310072767 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.262481 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0633082 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.78631e+06s, dt:60687.6s, Cycle: 124 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.45e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 6.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 7.30e-06 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-04 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 1.04e-04 ) ; + Last LinSolve(iter,res) = ( 6, 2.99e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14886369.130445452 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15216811.733596029 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 14470648.647987762 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.366078 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.065123 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.84699e+06s, dt:63643.7s, Cycle: 125 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 2.48e-08 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 6.29e-06 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.12e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.36e-03 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 2.36e-03 ) ; + Last LinSolve(iter,res) = ( 8, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.36e-06 ) ; ( Rwell ) = ( 2.18e-08 ) ; ( R ) = ( 4.36e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14930296.54060874 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15261441.356099378 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14516171.12536544 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.344297 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641495 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.91064e+06s, dt:67399.1s, Cycle: 126 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; ( R ) = ( 6.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.53e-06 ) ; ( R ) = ( 5.77e-02 ) ; + Last LinSolve(iter,res) = ( 8, 4.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-03 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 2.78e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.99e-06 ) ; ( Rwell ) = ( 2.78e-08 ) ; ( R ) = ( 3.99e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.05e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 14978483.014090203 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15309098.828152867 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14565610.383124707 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.353691 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753576 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.97804e+06s, dt:64127.1s, Cycle: 127 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.87e-02 ) ; ( Rwell ) = ( 2.40e-08 ) ; ( R ) = ( 5.87e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 1.48e-06 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-03 ) ; ( Rwell ) = ( 9.80e-08 ) ; ( R ) = ( 1.54e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.47e-06 ) ; ( Rwell ) = ( 3.17e-09 ) ; ( R ) = ( 1.47e-06 ) ; + Last LinSolve(iter,res) = ( 6, 7.39e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 15023523.308083212 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15354354.729961818 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls3: BHP (at the specified reference elevation): 14611928.998713467 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.332301 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0730658 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.04216e+06s, dt:62307.8s, Cycle: 128 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 8.03e-09 ) ; ( R ) = ( 6.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.07e-02 ) ; ( Rwell ) = ( 3.78e-06 ) ; ( R ) = ( 3.07e-02 ) ; + Last LinSolve(iter,res) = ( 4, 7.76e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.49e-03 ) ; ( Rwell ) = ( 2.45e-07 ) ; ( R ) = ( 1.49e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.51e-06 ) ; ( Rwell ) = ( 3.09e-09 ) ; ( R ) = ( 2.51e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.56e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15066627.10366838 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15397986.751375867 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 14656971.675511332 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294169 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694821 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.10447e+06s, dt:62616.6s, Cycle: 129 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.40e-02 ) ; ( Rwell ) = ( 7.93e-09 ) ; ( R ) = ( 6.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.53e-02 ) ; ( Rwell ) = ( 1.98e-06 ) ; ( R ) = ( 3.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.90e-03 ) ; ( Rwell ) = ( 2.00e-07 ) ; ( R ) = ( 4.90e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.17e-05 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 1.17e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.59e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15110520.993386492 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15442245.400847333 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 14702648.399332864 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.35342 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0700094 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.16709e+06s, dt:62611s, Cycle: 130 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.34e-02 ) ; ( Rwell ) = ( 1.22e-07 ) ; ( R ) = ( 6.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.21e-02 ) ; ( Rwell ) = ( 5.85e-06 ) ; ( R ) = ( 3.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.37e-05 ) ; ( Rwell ) = ( 4.81e-08 ) ; ( R ) = ( 6.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15154048.924345654 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15486050.860627918 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 14747244.363920579 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.312992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0722338 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.2297e+06s, dt:61306.7s, Cycle: 131 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.84e-02 ) ; ( Rwell ) = ( 5.14e-08 ) ; ( R ) = ( 5.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 2.90e-06 ) ; ( R ) = ( 4.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.77e-04 ) ; ( Rwell ) = ( 3.08e-07 ) ; ( R ) = ( 2.77e-04 ) ; + Last LinSolve(iter,res) = ( 7, 5.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15196385.00532196 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 15528298.00726191 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14790795.371685097 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.323562 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728292 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.29101e+06s, dt:59698.2s, Cycle: 132 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.20e-02 ) ; ( Rwell ) = ( 3.03e-07 ) ; ( R ) = ( 6.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.95e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; ( R ) = ( 3.95e-02 ) ; + Last LinSolve(iter,res) = ( 7, 5.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.56e-03 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 3.56e-03 ) ; + Last LinSolve(iter,res) = ( 8, 6.35e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.08e-06 ) ; ( Rwell ) = ( 8.86e-09 ) ; ( R ) = ( 7.08e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15237557.361464653 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 15569114.845858028 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 14833193.855662825 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.293958 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688421 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.3507e+06s, dt:60363.9s, Cycle: 133 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.44e-02 ) ; ( Rwell ) = ( 1.23e-08 ) ; ( R ) = ( 6.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.88e-02 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 2.88e-02 ) ; + Last LinSolve(iter,res) = ( 8, 5.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.23e-03 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 1.23e-03 ) ; + Last LinSolve(iter,res) = ( 9, 5.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.23e-06 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.23e-06 ) ; + Last LinSolve(iter,res) = ( 8, 1.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15279244.184562733 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 15610106.12646574 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 14875650.371707154 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.301616 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637249 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.41107e+06s, dt:64200.7s, Cycle: 134 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.61e-02 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 6.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 2.19e-06 ) ; ( R ) = ( 6.21e-02 ) ; + Last LinSolve(iter,res) = ( 7, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.69e-03 ) ; ( Rwell ) = ( 4.94e-07 ) ; ( R ) = ( 4.69e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.18e-06 ) ; ( Rwell ) = ( 1.04e-08 ) ; ( R ) = ( 5.18e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15323629.427804051 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15654055.528772378 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 14921693.549978824 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324588 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0644776 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.47527e+06s, dt:67764.8s, Cycle: 135 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.32e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 6.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-02 ) ; ( Rwell ) = ( 1.98e-06 ) ; ( R ) = ( 1.78e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.97e-04 ) ; ( Rwell ) = ( 3.32e-07 ) ; ( R ) = ( 9.97e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15369671.606883293 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15699893.742254697 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 14969476.325854074 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320515 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662952 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.54303e+06s, dt:70243.2s, Cycle: 136 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; ( R ) = ( 6.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.47e-06 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.26e-03 ) ; ( Rwell ) = ( 8.51e-07 ) ; ( R ) = ( 6.26e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15416858.643817697 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 15748187.585671792 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15018430.346229922 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324685 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721314 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.61328e+06s, dt:68845.8s, Cycle: 137 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.03e-02 ) ; ( Rwell ) = ( 1.85e-07 ) ; ( R ) = ( 6.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 1.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.69e-05 ) ; ( Rwell ) = ( 3.45e-07 ) ; ( R ) = ( 7.69e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15462657.482362097 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 15794163.377590818 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 15065700.509505054 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320569 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0696781 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.68212e+06s, dt:69057.5s, Cycle: 138 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 3.40e-07 ) ; ( R ) = ( 6.30e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.05e-04 ) ; ( Rwell ) = ( 2.56e-07 ) ; ( R ) = ( 4.05e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15508130.240315957 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 15839184.069017056 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 15112151.203341829 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324258 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0646401 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.75118e+06s, dt:72772.3s, Cycle: 139 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.47e-02 ) ; ( Rwell ) = ( 2.58e-07 ) ; ( R ) = ( 6.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.78e-02 ) ; ( Rwell ) = ( 2.84e-06 ) ; ( R ) = ( 3.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-03 ) ; ( Rwell ) = ( 5.34e-07 ) ; ( R ) = ( 4.51e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.08e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.86e-05 ) ; ( Rwell ) = ( 2.59e-08 ) ; ( R ) = ( 1.86e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15555208.427350774 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15886533.517030891 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15160494.723243712 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.334801 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0562203 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.82395e+06s, dt:83765.2s, Cycle: 140 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 2.59e-08 ) ; ( R ) = ( 6.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 1.09e-01 ) ; + Last LinSolve(iter,res) = ( 6, 4.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.96e-02 ) ; ( Rwell ) = ( 5.84e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.33e-03 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 5.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-05 ) ; ( Rwell ) = ( 8.11e-09 ) ; ( R ) = ( 1.82e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15608760.789222559 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 15940414.481736448 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 15215580.471480945 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.359192 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0892052 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 4.90772e+06s, dt:70813s, Cycle: 141 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.95e-02 ) ; ( Rwell ) = ( 1.28e-08 ) ; ( R ) = ( 5.95e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 2.26e-06 ) ; ( R ) = ( 4.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.82e-08 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 7, 5.39e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.83e-06 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 6.83e-06 ) ; + Last LinSolve(iter,res) = ( 4, 2.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15653773.438902719 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 15986974.636191037 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 15262129.6018317 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.322403 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0687801 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 4.97853e+06s, dt:71645.4s, Cycle: 142 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.77e-02 ) ; ( Rwell ) = ( 1.81e-08 ) ; ( R ) = ( 5.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.10e-06 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.16e-04 ) ; ( Rwell ) = ( 2.66e-07 ) ; ( R ) = ( 6.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15698727.924421888 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 16033218.125276769 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15308581.481010806 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294291 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0596002 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.05018e+06s, dt:79521.7s, Cycle: 143 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.68e-07 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.27e-02 ) ; ( Rwell ) = ( 4.55e-06 ) ; ( R ) = ( 5.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.08e-03 ) ; ( Rwell ) = ( 2.19e-07 ) ; ( R ) = ( 3.08e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.16e-05 ) ; ( Rwell ) = ( 4.10e-09 ) ; ( R ) = ( 5.16e-05 ) ; + Last LinSolve(iter,res) = ( 6, 1.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15747881.47755418 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 16083383.570053458 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15359222.951793108 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308101 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0627385 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.1297e+06s, dt:85429.9s, Cycle: 144 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 6.53e-09 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.82e-06 ) ; ( R ) = ( 3.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.23e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.72e-04 ) ; ( Rwell ) = ( 1.59e-07 ) ; ( R ) = ( 6.72e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.91e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15800485.264042016 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 16136681.863083825 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 15413269.651286839 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.389574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0674022 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.21513e+06s, dt:87597.1s, Cycle: 145 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.75e-02 ) ; ( Rwell ) = ( 1.61e-07 ) ; ( R ) = ( 5.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.91e-02 ) ; ( Rwell ) = ( 2.07e-06 ) ; ( R ) = ( 4.91e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.96e-03 ) ; ( Rwell ) = ( 5.58e-07 ) ; ( R ) = ( 3.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.50e-05 ) ; ( Rwell ) = ( 8.76e-09 ) ; ( R ) = ( 1.50e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15855210.801916944 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 16190887.355444716 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 15469065.18560786 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668393 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.30272e+06s, dt:90315.7s, Cycle: 146 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 8.01e-09 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.58e-06 ) ; ( R ) = ( 4.29e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.59e-04 ) ; ( Rwell ) = ( 5.97e-08 ) ; ( R ) = ( 3.59e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15911371.526493661 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16246610.546115935 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 15526354.511404896 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.351983 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0902922 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.39304e+06s, dt:75688.2s, Cycle: 147 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 6.39e-08 ) ; ( R ) = ( 5.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.50e-02 ) ; ( Rwell ) = ( 2.43e-06 ) ; ( R ) = ( 2.50e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.03e-03 ) ; ( Rwell ) = ( 1.72e-07 ) ; ( R ) = ( 2.03e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 1.66e-08 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 15957275.342839258 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 16292870.69317122 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 15573482.008542515 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668366 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.46873e+06s, dt:78039.4s, Cycle: 148 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.92e-06 ) ; ( R ) = ( 2.33e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-04 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 8.44e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16003805.430201665 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 16340068.0379005 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15621348.898785252 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.302937 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0568969 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.54677e+06s, dt:89166.6s, Cycle: 149 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.60e-02 ) ; ( Rwell ) = ( 4.18e-08 ) ; ( R ) = ( 5.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 1.40e-06 ) ; ( R ) = ( 4.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.58e-03 ) ; ( Rwell ) = ( 1.83e-07 ) ; ( R ) = ( 3.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.70e-06 ) ; ( Rwell ) = ( 4.50e-08 ) ; ( R ) = ( 4.70e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.82e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16056382.024531502 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16393910.994062753 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 15675123.485794049 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.367065 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0653787 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.63593e+06s, dt:93271.7s, Cycle: 150 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 4.21e-08 ) ; ( R ) = ( 5.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.29e-06 ) ; ( R ) = ( 5.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.79e-07 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.04e-05 ) ; ( Rwell ) = ( 8.09e-08 ) ; ( R ) = ( 5.04e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16112119.793029426 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16450352.945468847 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15732015.211798064 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369294 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0792025 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.72921e+06s, dt:85755.8s, Cycle: 151 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.56e-02 ) ; ( Rwell ) = ( 8.32e-08 ) ; ( R ) = ( 5.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.96e-02 ) ; ( Rwell ) = ( 4.66e-06 ) ; ( R ) = ( 2.96e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.31e-04 ) ; ( Rwell ) = ( 2.61e-07 ) ; ( R ) = ( 6.31e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16163386.15469336 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16502027.320008637 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 15784414.551123235 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.310582 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0686688 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.81496e+06s, dt:86857s, Cycle: 152 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 2.57e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.77e-02 ) ; ( Rwell ) = ( 8.97e-07 ) ; ( R ) = ( 3.77e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.32e-04 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 4.32e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.42e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16215746.627679212 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 16553861.516249798 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 15837184.675823225 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.321949 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0701116 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 5.90182e+06s, dt:86764.8s, Cycle: 153 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.99e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 5.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 6.78e-07 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.81e-05 ) ; ( Rwell ) = ( 4.57e-08 ) ; ( R ) = ( 6.81e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16267285.392045256 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16605092.036640229 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 15889495.49939927 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.315183 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671334 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 5.98858e+06s, dt:89200s, Cycle: 154 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.21e-02 ) ; ( Rwell ) = ( 4.59e-08 ) ; ( R ) = ( 6.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.54e-02 ) ; ( Rwell ) = ( 1.20e-06 ) ; ( R ) = ( 3.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.40e-04 ) ; ( Rwell ) = ( 7.64e-08 ) ; ( R ) = ( 8.40e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16320992.744121088 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 16658642.863658601 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 15944616.019622577 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.345773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0751002 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.07778e+06s, dt:85068s, Cycle: 155 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.62e-02 ) ; ( Rwell ) = ( 7.64e-08 ) ; ( R ) = ( 5.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 2.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.12e-03 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 3.12e-03 ) ; + Last LinSolve(iter,res) = ( 3, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.35e-06 ) ; ( Rwell ) = ( 1.42e-08 ) ; ( R ) = ( 8.35e-06 ) ; + Last LinSolve(iter,res) = ( 4, 6.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16372221.520865634 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 16709676.724625992 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 15997275.960209737 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.324393 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777723 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.16285e+06s, dt:79205s, Cycle: 156 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.65e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 5.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 1.25e-06 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.37e-02 ) ; ( Rwell ) = ( 6.21e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.29e-03 ) ; ( Rwell ) = ( 6.93e-07 ) ; ( R ) = ( 6.29e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.43e-05 ) ; ( Rwell ) = ( 7.00e-08 ) ; ( R ) = ( 3.43e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16419690.057989871 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 16757030.48924207 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 16045982.714074152 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279591 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0727534 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.24206e+06s, dt:77181.1s, Cycle: 157 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.83e-02 ) ; ( Rwell ) = ( 7.38e-08 ) ; ( R ) = ( 5.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.25e-03 ) ; ( Rwell ) = ( 2.57e-06 ) ; ( R ) = ( 4.25e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.77e-05 ) ; ( Rwell ) = ( 8.69e-08 ) ; ( R ) = ( 1.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16464682.23390435 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 16802202.14637973 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 16092031.943406777 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.270981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672504 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.31924e+06s, dt:79256.5s, Cycle: 158 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 8.91e-08 ) ; ( R ) = ( 5.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 7.59e-07 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.82e-03 ) ; ( Rwell ) = ( 1.97e-07 ) ; ( R ) = ( 9.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.24e-05 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 2.24e-05 ) ; + Last LinSolve(iter,res) = ( 3, 3.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16509851.652552592 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 16848084.749950267 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 16138346.470788458 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.276336 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0617854 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.39849e+06s, dt:85983.4s, Cycle: 159 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.07e-02 ) ; ( Rwell ) = ( 3.51e-08 ) ; ( R ) = ( 6.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.76e-02 ) ; ( Rwell ) = ( 1.16e-06 ) ; ( R ) = ( 3.76e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.49e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.63e-03 ) ; ( Rwell ) = ( 4.68e-08 ) ; ( R ) = ( 4.63e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.69e-05 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 3.69e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.33e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16558430.486321826 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 16897715.948618323 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 16188355.589598557 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.296863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0561331 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.48448e+06s, dt:99066.7s, Cycle: 160 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.11e-02 ) ; ( Rwell ) = ( 1.94e-08 ) ; ( R ) = ( 6.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 7.29e-07 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.44e-03 ) ; ( Rwell ) = ( 4.30e-08 ) ; ( R ) = ( 2.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.05e-06 ) ; ( Rwell ) = ( 3.93e-08 ) ; ( R ) = ( 4.05e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16615179.825879112 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 16954182.81430578 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16246607.99882983 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.337466 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607346 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.58354e+06s, dt:108655s, Cycle: 161 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.70e-02 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 5.70e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.04e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 7.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.77e-02 ) ; ( Rwell ) = ( 6.68e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.09e-02 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 8.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.72e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.83e-02 ) ; ( Rwell ) = ( 5.53e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.08e-02 ) ; ( Rwell ) = ( 4.71e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.00e-03 ) ; ( Rwell ) = ( 7.35e-07 ) ; ( R ) = ( 6.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.25e-05 ) ; ( Rwell ) = ( 1.50e-08 ) ; ( R ) = ( 1.25e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.52e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16676631.573181104 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17015114.435654465 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16309313.021258594 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.379902 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762995 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.6922e+06s, dt:102505s, Cycle: 162 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 1.73e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.03e-02 ) ; ( Rwell ) = ( 2.01e-06 ) ; ( R ) = ( 3.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.69e-04 ) ; ( Rwell ) = ( 1.03e-07 ) ; ( R ) = ( 1.69e-04 ) ; + Last LinSolve(iter,res) = ( 6, 7.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16734186.455653653 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 17072940.690240577 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16368310.643988878 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.350542 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0794866 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.7947e+06s, dt:94011s, Cycle: 163 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.59e-02 ) ; ( Rwell ) = ( 1.00e-07 ) ; ( R ) = ( 5.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 2.51e-06 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-04 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 1.36e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16787078.71028531 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 17125796.50836143 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 16422379.394209972 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.322028 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0733787 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 6.88872e+06s, dt:91080.2s, Cycle: 164 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.73e-02 ) ; ( Rwell ) = ( 2.01e-07 ) ; ( R ) = ( 5.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.23e-02 ) ; ( Rwell ) = ( 2.21e-06 ) ; ( R ) = ( 7.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.39e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.74e-02 ) ; ( Rwell ) = ( 1.10e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.36e-03 ) ; ( Rwell ) = ( 6.58e-07 ) ; ( R ) = ( 1.36e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.54e-06 ) ; ( Rwell ) = ( 2.82e-09 ) ; ( R ) = ( 3.54e-06 ) ; + Last LinSolve(iter,res) = ( 7, 6.86e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 16837404.73399263 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 17176093.019651346 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 16473918.761772873 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299154 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0666001 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 6.9798e+06s, dt:94128.1s, Cycle: 165 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.82e-02 ) ; ( Rwell ) = ( 5.10e-09 ) ; ( R ) = ( 5.82e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 1.44e-06 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.85e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.81e-02 ) ; ( Rwell ) = ( 7.23e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 8.59e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 7.28e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 7.25e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.88e-02 ) ; ( Rwell ) = ( 5.70e-07 ) ; ( R ) = ( 1.88e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 6.60e-04 ) ; ( Rwell ) = ( 2.27e-07 ) ; ( R ) = ( 6.60e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 16888156.089273307 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 17227018.837946262 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 16526107.180299439 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.29425 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602306 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.07392e+06s, dt:103784s, Cycle: 166 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.86e-02 ) ; ( Rwell ) = ( 2.28e-07 ) ; ( R ) = ( 5.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 1.75e-06 ) ; ( R ) = ( 4.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.38e-03 ) ; ( Rwell ) = ( 5.51e-07 ) ; ( R ) = ( 1.38e-03 ) ; + Last LinSolve(iter,res) = ( 4, 3.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.08e-07 ) ; ( Rwell ) = ( 7.00e-10 ) ; ( R ) = ( 8.08e-07 ) ; + Last LinSolve(iter,res) = ( 6, 8.98e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 16943502.39921584 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17282328.1941993 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 16582896.188485742 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0619011 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.17771e+06s, dt:112459s, Cycle: 167 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.39e-02 ) ; ( Rwell ) = ( 4.64e-09 ) ; ( R ) = ( 5.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.55e-02 ) ; ( Rwell ) = ( 5.22e-07 ) ; ( R ) = ( 6.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.66e-02 ) ; ( Rwell ) = ( 2.65e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.02e-07 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.76e-02 ) ; ( Rwell ) = ( 1.07e-06 ) ; ( R ) = ( 1.76e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.67e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.18e-05 ) ; ( Rwell ) = ( 1.84e-07 ) ; ( R ) = ( 4.18e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17003178.407949835 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 17342801.47910604 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 16644669.610686496 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346133 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069576 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.29017e+06s, dt:112914s, Cycle: 168 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.81e-07 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.53e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 5.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.29e-02 ) ; ( Rwell ) = ( 5.42e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.12e-03 ) ; ( Rwell ) = ( 2.76e-08 ) ; ( R ) = ( 1.12e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.66e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.63e-06 ) ; ( Rwell ) = ( 5.04e-09 ) ; ( R ) = ( 1.63e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17064026.22608907 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17404270.37548236 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16707250.028529592 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.347303 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0725904 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.40308e+06s, dt:110196s, Cycle: 169 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 4.65e-09 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.59e-02 ) ; ( Rwell ) = ( 5.17e-07 ) ; ( R ) = ( 1.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.08e-04 ) ; ( Rwell ) = ( 5.99e-08 ) ; ( R ) = ( 6.08e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17123362.657258365 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 17463428.83284779 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 16767683.216238525 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.318813 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0749344 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.51328e+06s, dt:105250s, Cycle: 170 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 5.85e-08 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.62e-06 ) ; ( R ) = ( 4.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.50e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.11e-04 ) ; ( Rwell ) = ( 4.46e-07 ) ; ( R ) = ( 2.11e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17180169.233131424 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 17519629.026802197 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16825253.305006776 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.340484 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.075735 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.61853e+06s, dt:99798.8s, Cycle: 171 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.38e-02 ) ; ( Rwell ) = ( 4.46e-07 ) ; ( R ) = ( 5.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.42e-02 ) ; ( Rwell ) = ( 1.18e-06 ) ; ( R ) = ( 1.42e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.18e-04 ) ; ( Rwell ) = ( 5.02e-08 ) ; ( R ) = ( 2.18e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17234076.28164461 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17572968.399522863 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 16880038.05687686 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.302115 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0814021 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.71833e+06s, dt:90023s, Cycle: 172 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 4.79e-08 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 1.82e-06 ) ; ( R ) = ( 4.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 1.44e-07 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.96e-04 ) ; ( Rwell ) = ( 1.17e-08 ) ; ( R ) = ( 3.96e-04 ) ; + Last LinSolve(iter,res) = ( 2, 9.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17282536.344845634 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17621616.250400472 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 16929549.777725313 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.28532 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0758887 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 7.80835e+06s, dt:85242.4s, Cycle: 173 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 1.49e-08 ) ; ( R ) = ( 5.57e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.19e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.05e-04 ) ; ( Rwell ) = ( 1.29e-07 ) ; ( R ) = ( 1.05e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17327856.505670793 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17667319.75225472 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 16975761.2700196 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.259496 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069401 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.89359e+06s, dt:85731.5s, Cycle: 174 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.69e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 5.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.65e-03 ) ; ( Rwell ) = ( 7.11e-07 ) ; ( R ) = ( 5.65e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.12e-05 ) ; ( Rwell ) = ( 7.15e-08 ) ; ( R ) = ( 2.12e-05 ) ; + Last LinSolve(iter,res) = ( 5, 4.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17372695.002812695 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17712305.005370524 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 17021323.916458696 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255989 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0632554 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 7.97932e+06s, dt:91616.4s, Cycle: 175 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.76e-02 ) ; ( Rwell ) = ( 6.92e-08 ) ; ( R ) = ( 5.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.99e-02 ) ; ( Rwell ) = ( 5.15e-06 ) ; ( R ) = ( 2.99e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 1.35e-07 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17419981.107448537 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 17759527.780425873 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 17069387.657947436 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266698 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0546621 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.07094e+06s, dt:107289s, Cycle: 176 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.64e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 5.64e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.26e-01 ) ; ( Rwell ) = ( 1.45e-06 ) ; ( R ) = ( 1.26e-01 ) ; + Last LinSolve(iter,res) = ( 5, 5.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.65e-02 ) ; ( Rwell ) = ( 6.57e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.52e-02 ) ; ( Rwell ) = ( 2.62e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.13e-06 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 1.91e-07 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.10e-06 ) ; ( Rwell ) = ( 3.11e-09 ) ; ( R ) = ( 1.10e-06 ) ; + Last LinSolve(iter,res) = ( 6, 9.62e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 17475309.357362114 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 17814579.858774222 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 17125696.404909458 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.312175 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0526631 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.17823e+06s, dt:128507s, Cycle: 177 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 5.05e-09 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 2.32e-06 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.74e-04 ) ; ( Rwell ) = ( 1.62e-07 ) ; ( R ) = ( 2.74e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17541720.284557555 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 17880594.853958935 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17193256.289509416 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.369375 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0576558 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 8.30673e+06s, dt:145627s, Cycle: 178 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.17e-02 ) ; ( Rwell ) = ( 1.63e-07 ) ; ( R ) = ( 5.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.67e-02 ) ; ( Rwell ) = ( 1.04e-06 ) ; ( R ) = ( 6.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 5.41e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.29e-04 ) ; ( Rwell ) = ( 2.85e-07 ) ; ( R ) = ( 1.29e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.08e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17617293.307911225 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 17955997.777289443 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17270297.421035886 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.415802 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0785426 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.45236e+06s, dt:134671s, Cycle: 179 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.01e-02 ) ; ( Rwell ) = ( 2.85e-07 ) ; ( R ) = ( 5.01e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.26e-06 ) ; ( R ) = ( 4.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.96e-04 ) ; ( Rwell ) = ( 2.41e-07 ) ; ( R ) = ( 9.96e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17687346.88867736 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 18025593.18997505 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 17341827.58425523 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.381975 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777844 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.58703e+06s, dt:125376s, Cycle: 180 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.11e-02 ) ; ( Rwell ) = ( 2.41e-07 ) ; ( R ) = ( 5.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 2.98e-06 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.55e-04 ) ; ( Rwell ) = ( 3.41e-07 ) ; ( R ) = ( 7.55e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17751730.759954188 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 18089415.10617658 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17406997.79674083 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.360482 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0911079 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.71241e+06s, dt:104390s, Cycle: 181 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 3.42e-07 ) ; ( R ) = ( 5.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.37e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; ( R ) = ( 3.37e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-03 ) ; ( Rwell ) = ( 3.97e-07 ) ; ( R ) = ( 1.86e-03 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.46e-06 ) ; ( Rwell ) = ( 2.17e-09 ) ; ( R ) = ( 1.46e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17804888.576541513 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 18142333.683897763 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 17461013.463778228 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0801288 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.8168e+06s, dt:95206.2s, Cycle: 182 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.22e-02 ) ; ( Rwell ) = ( 4.00e-09 ) ; ( R ) = ( 5.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.02e-02 ) ; ( Rwell ) = ( 2.13e-06 ) ; ( R ) = ( 3.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-05 ) ; ( Rwell ) = ( 1.14e-07 ) ; ( R ) = ( 6.11e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.46e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17853335.48551722 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 18190787.711830627 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 17510377.286605075 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728816 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 8.912e+06s, dt:92663.2s, Cycle: 183 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.31e-02 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 5.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.97e-02 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 1.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.22e-04 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 1.22e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17900526.389935218 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 18237566.256361365 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 17558463.87807666 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.275992 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0694347 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.00467e+06s, dt:93164.8s, Cycle: 184 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.45e-02 ) ; ( Rwell ) = ( 1.17e-07 ) ; ( R ) = ( 5.45e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.11e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 2.11e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.07e-05 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 4.07e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17947858.457768973 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 18284360.796142913 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 17606762.322695814 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281357 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736767 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.09783e+06s, dt:90012.9s, Cycle: 185 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.21e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 5.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.81e-02 ) ; ( Rwell ) = ( 1.68e-06 ) ; ( R ) = ( 3.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.44e-04 ) ; ( Rwell ) = ( 1.02e-07 ) ; ( R ) = ( 3.44e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.84e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 17993222.81800419 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 18329476.225514896 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 17652981.94395687 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266402 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0720266 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.18785e+06s, dt:88308.5s, Cycle: 186 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.42e-02 ) ; ( Rwell ) = ( 1.04e-07 ) ; ( R ) = ( 5.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.97e-02 ) ; ( Rwell ) = ( 5.13e-07 ) ; ( R ) = ( 5.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.27e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.92e-02 ) ; ( Rwell ) = ( 3.09e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.79e-03 ) ; ( Rwell ) = ( 2.82e-07 ) ; ( R ) = ( 1.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-06 ) ; ( Rwell ) = ( 1.59e-08 ) ; ( R ) = ( 2.47e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18037156.359533917 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 18373293.629240546 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 17697719.093093757 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250426 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0664707 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.27615e+06s, dt:91379.9s, Cycle: 187 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.51e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 5.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 5.21e-07 ) ; ( R ) = ( 4.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-04 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 2.07e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.17e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18081974.5293232 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 18418092.842188805 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17743366.567119647 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250517 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588045 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.36753e+06s, dt:102286s, Cycle: 188 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.48e-02 ) ; ( Rwell ) = ( 9.83e-08 ) ; ( R ) = ( 5.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 2.47e-06 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.48e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.57e-02 ) ; ( Rwell ) = ( 1.18e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 4.12e-02 ) ; ( Rwell ) = ( 5.43e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.13e-02 ) ; ( Rwell ) = ( 1.51e-06 ) ; ( R ) = ( 9.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.15e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 7.86e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 6.65e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 6.04e-07 ) ; + Line search failed to produce reduced residual. Accepting iteration. + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.48e-02 ) ; ( Rwell ) = ( 1.44e-06 ) ; ( R ) = ( 2.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 4.09e-04 ) ; ( Rwell ) = ( 7.60e-08 ) ; ( R ) = ( 4.09e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18131809.621656686 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 18468129.947450638 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 17794010.377150163 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278322 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0551266 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.46982e+06s, dt:119166s, Cycle: 189 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 7.83e-08 ) ; ( R ) = ( 5.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.58e-02 ) ; ( Rwell ) = ( 2.50e-06 ) ; ( R ) = ( 3.58e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.78e-04 ) ; ( Rwell ) = ( 8.32e-08 ) ; ( R ) = ( 5.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18189283.331875775 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 18525248.60842841 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 17852219.670575988 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.32666 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0798331 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.58899e+06s, dt:108962s, Cycle: 190 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.89e-02 ) ; ( Rwell ) = ( 8.54e-08 ) ; ( R ) = ( 4.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.89e-02 ) ; ( Rwell ) = ( 2.90e-06 ) ; ( R ) = ( 2.89e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.17e-04 ) ; ( Rwell ) = ( 1.57e-07 ) ; ( R ) = ( 2.17e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18241540.69014383 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 18577148.429481223 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 17905154.738698512 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.292746 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0777985 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.69795e+06s, dt:101429s, Cycle: 191 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.55e-07 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; ( R ) = ( 3.09e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 4.95e-07 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18289962.003443226 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 18625217.251734972 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 17954215.563862637 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260186 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0703311 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 9.79938e+06s, dt:101110s, Cycle: 192 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 4.95e-07 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.92e-06 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.70e-03 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 5.70e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.34e-04 ) ; ( Rwell ) = ( 6.07e-08 ) ; ( R ) = ( 1.34e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18337873.628342073 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 18672803.74366999 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 18002995.297686394 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.256076 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0643202 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 9.90049e+06s, dt:106892s, Cycle: 193 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 5.89e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.28e-02 ) ; ( Rwell ) = ( 4.58e-07 ) ; ( R ) = ( 3.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.25e-04 ) ; ( Rwell ) = ( 8.71e-08 ) ; ( R ) = ( 8.25e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.43e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18388918.363641217 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 18723453.445938323 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 18054839.133496094 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274283 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0585915 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.00074e+07s, dt:119922s, Cycle: 194 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.14e-02 ) ; ( Rwell ) = ( 8.92e-08 ) ; ( R ) = ( 5.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.54e-02 ) ; ( Rwell ) = ( 5.26e-07 ) ; ( R ) = ( 2.54e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.16e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.06e-03 ) ; ( Rwell ) = ( 1.44e-07 ) ; ( R ) = ( 2.06e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.71e-06 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 2.71e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18446160.562450435 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +wellControls2: BHP (at the specified reference elevation): 18780191.505812816 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 18112850.588830706 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307366 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0668793 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.01273e+07s, dt:123595s, Cycle: 195 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 9.42e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.32e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 5.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.40e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 5.33e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 2.67e-07 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-05 ) ; ( Rwell ) = ( 2.86e-08 ) ; ( R ) = ( 1.92e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18504792.71153116 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 18838440.841607653 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 18172149.975111227 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308171 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0659999 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.02509e+07s, dt:128490s, Cycle: 196 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 2.61e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.52e-02 ) ; ( Rwell ) = ( 5.33e-07 ) ; ( R ) = ( 1.52e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-04 ) ; ( Rwell ) = ( 6.73e-08 ) ; ( R ) = ( 1.08e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18565013.73569213 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 18897946.538999323 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 18232961.6045098 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.311582 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0602777 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.03794e+07s, dt:141602s, Cycle: 197 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.62e-02 ) ; ( Rwell ) = ( 6.55e-08 ) ; ( R ) = ( 4.62e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.99e-02 ) ; ( Rwell ) = ( 5.17e-07 ) ; ( R ) = ( 4.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.33e-02 ) ; ( Rwell ) = ( 2.51e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.42e-03 ) ; ( Rwell ) = ( 5.36e-07 ) ; ( R ) = ( 7.42e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.47e-05 ) ; ( Rwell ) = ( 1.14e-07 ) ; ( R ) = ( 2.47e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18630971.990420613 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 18963542.15779206 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 18299885.72901066 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.341492 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0607882 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.0521e+07s, dt:155219s, Cycle: 198 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.85e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 8.85e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.22e-02 ) ; ( Rwell ) = ( 9.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.65e-02 ) ; ( Rwell ) = ( 2.94e-07 ) ; ( R ) = ( 8.65e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.63e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.55e-02 ) ; ( Rwell ) = ( 6.00e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 7.53e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.60e-02 ) ; ( Rwell ) = ( 1.75e-07 ) ; ( R ) = ( 8.60e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.64e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 4.64e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 6.08e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 6.81e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 1.62e-02 ) ; ( Rwell ) = ( 7.17e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 2.04e-07 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 5 + ( Rflow ) = ( 3.90e-05 ) ; ( Rwell ) = ( 1.65e-08 ) ; ( R ) = ( 3.90e-05 ) ; + Last LinSolve(iter,res) = ( 6, 5.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18703751.658490162 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 19035523.23390971 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 18373334.880323384 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.365034 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774239 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.06762e+07s, dt:144969s, Cycle: 199 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 1.65e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.19e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 8.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.56e-02 ) ; ( Rwell ) = ( 6.92e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 8.09e-07 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.43e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.30e-04 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 1.30e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18771734.78295531 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 19102907.72302304 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 18442140.33973722 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.349088 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774721 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.08212e+07s, dt:135338s, Cycle: 200 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.93e-02 ) ; ( Rwell ) = ( 2.14e-07 ) ; ( R ) = ( 4.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.37e-02 ) ; ( Rwell ) = ( 4.76e-07 ) ; ( R ) = ( 2.37e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 3.78e-08 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.81e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18834145.833719302 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19164990.48031982 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 18505412.498237416 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.330253 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0732024 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.09565e+07s, dt:131333s, Cycle: 201 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.05e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; ( R ) = ( 5.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 5.37e-07 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.81e-04 ) ; ( Rwell ) = ( 2.97e-07 ) ; ( R ) = ( 2.81e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.88e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18894161.258638628 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 19224729.461585402 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 18566245.352304116 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.323945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682303 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.10878e+07s, dt:133584s, Cycle: 202 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.10e-02 ) ; ( Rwell ) = ( 2.97e-07 ) ; ( R ) = ( 5.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.69e-02 ) ; ( Rwell ) = ( 6.44e-07 ) ; ( R ) = ( 1.69e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.61e-03 ) ; ( Rwell ) = ( 8.86e-08 ) ; ( R ) = ( 3.61e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.22e-05 ) ; ( Rwell ) = ( 1.70e-08 ) ; ( R ) = ( 1.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 18955400.559826598 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 19285216.834178574 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 18628339.90241917 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.329066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0718764 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.12214e+07s, dt:131239s, Cycle: 203 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 1.55e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-01 ) ; ( Rwell ) = ( 5.62e-07 ) ; ( R ) = ( 1.95e-01 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 7.81e-02 ) ; ( Rwell ) = ( 2.66e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 1.34e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.86e-02 ) ; ( Rwell ) = ( 4.66e-07 ) ; ( R ) = ( 1.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.59e-05 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 1.59e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.58e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19015453.949442945 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 19344486.8971354 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 18689093.70018288 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.317381 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0692362 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.13527e+07s, dt:132200s, Cycle: 204 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.08e-02 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 5.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.73e-02 ) ; ( Rwell ) = ( 6.58e-07 ) ; ( R ) = ( 2.73e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.06e-03 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 4.06e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-05 ) ; ( Rwell ) = ( 1.77e-08 ) ; ( R ) = ( 1.01e-05 ) ; + Last LinSolve(iter,res) = ( 3, 6.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19075948.921386205 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 19404301.932235632 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 18750181.081751414 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.313232 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.064528 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.14849e+07s, dt:139469s, Cycle: 205 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.13e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 5.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 8.28e-07 ) ; ( R ) = ( 4.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.02e-04 ) ; ( Rwell ) = ( 2.73e-07 ) ; ( R ) = ( 2.02e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19139632.90205272 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 19467480.625971004 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 18814524.606943604 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.335552 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0736475 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.16243e+07s, dt:134787s, Cycle: 206 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.44e-02 ) ; ( Rwell ) = ( 2.73e-07 ) ; ( R ) = ( 4.44e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.59e-02 ) ; ( Rwell ) = ( 5.32e-07 ) ; ( R ) = ( 2.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.53e-03 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 1.53e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.56e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.13e-06 ) ; ( Rwell ) = ( 7.77e-10 ) ; ( R ) = ( 2.13e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19201767.29521002 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 19528690.729746073 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 18877188.10297039 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.329717 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697335 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.17591e+07s, dt:135129s, Cycle: 207 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.50e-02 ) ; ( Rwell ) = ( 2.85e-09 ) ; ( R ) = ( 4.50e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.92e-02 ) ; ( Rwell ) = ( 5.41e-07 ) ; ( R ) = ( 1.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.01e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.14e-05 ) ; ( Rwell ) = ( 1.40e-08 ) ; ( R ) = ( 4.14e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19262955.076106925 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19589143.834852904 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 18938892.467788838 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.320741 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0618974 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.18943e+07s, dt:146429s, Cycle: 208 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 1.53e-08 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.57e-02 ) ; ( Rwell ) = ( 8.43e-07 ) ; ( R ) = ( 3.57e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.25e-02 ) ; ( Rwell ) = ( 3.32e-08 ) ; ( R ) = ( 3.25e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.46e-05 ) ; ( Rwell ) = ( 9.03e-08 ) ; ( R ) = ( 3.46e-05 ) ; + Last LinSolve(iter,res) = ( 3, 4.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19328681.90009088 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19654477.272759188 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 19005331.509521212 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.330681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066285 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.20407e+07s, dt:151800s, Cycle: 209 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.76e-02 ) ; ( Rwell ) = ( 9.13e-08 ) ; ( R ) = ( 4.76e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 4.32e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.56e-03 ) ; ( Rwell ) = ( 4.81e-08 ) ; ( R ) = ( 4.56e-03 ) ; + Last LinSolve(iter,res) = ( 6, 3.71e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.57e-06 ) ; ( Rwell ) = ( 4.02e-09 ) ; ( R ) = ( 8.57e-06 ) ; + Last LinSolve(iter,res) = ( 3, 4.68e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19396424.57342305 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 19721928.021107808 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 19073942.9186941 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.333046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0690469 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.21925e+07s, dt:153190s, Cycle: 210 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.69e-02 ) ; ( Rwell ) = ( 5.28e-09 ) ; ( R ) = ( 4.69e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.18e-02 ) ; ( Rwell ) = ( 1.53e-06 ) ; ( R ) = ( 1.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.01e-03 ) ; ( Rwell ) = ( 3.57e-08 ) ; ( R ) = ( 5.01e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.80e-05 ) ; ( Rwell ) = ( 3.45e-08 ) ; ( R ) = ( 2.80e-05 ) ; + Last LinSolve(iter,res) = ( 3, 5.57e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19464433.95074377 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 19789215.47862211 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 19142724.871691793 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.336618 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0685314 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.23457e+07s, dt:155363s, Cycle: 211 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.73e-02 ) ; ( Rwell ) = ( 3.56e-08 ) ; ( R ) = ( 4.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.67e-01 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 1.67e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.19e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.02e-02 ) ; ( Rwell ) = ( 8.04e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 4.84e-07 ) ; ( R ) = ( 2.05e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.92e-04 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 1.92e-04 ) ; + Last LinSolve(iter,res) = ( 6, 3.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19534345.40577785 Pa +wellControls1: Total rate: 56.32837354192298 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +wellControls2: BHP (at the specified reference elevation): 19858150.12306143 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 19213455.50249326 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.347908 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0890164 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.2501e+07s, dt:131540s, Cycle: 212 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 4.49e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.00e-01 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 1.00e-01 ) ; + Last LinSolve(iter,res) = ( 5, 8.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 5.46e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.11e-03 ) ; ( Rwell ) = ( 4.85e-07 ) ; ( R ) = ( 6.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.66e-06 ) ; ( Rwell ) = ( 7.51e-09 ) ; ( R ) = ( 5.66e-06 ) ; + Last LinSolve(iter,res) = ( 5, 5.00e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19593583.287423227 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 19916461.81570751 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 19273199.34995624 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.287241 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755333 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.26326e+07s, dt:124955s, Cycle: 213 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.48e-02 ) ; ( Rwell ) = ( 6.24e-09 ) ; ( R ) = ( 4.48e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.67e-02 ) ; ( Rwell ) = ( 6.45e-07 ) ; ( R ) = ( 2.67e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.04e-05 ) ; ( Rwell ) = ( 1.12e-07 ) ; ( R ) = ( 4.04e-05 ) ; + Last LinSolve(iter,res) = ( 5, 9.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19649317.979580443 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 19971593.338247508 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 19329465.424672 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.26526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637888 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.27575e+07s, dt:132812s, Cycle: 214 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.37e-02 ) ; ( Rwell ) = ( 1.10e-07 ) ; ( R ) = ( 4.37e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 6.34e-07 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.90e-03 ) ; ( Rwell ) = ( 1.56e-07 ) ; ( R ) = ( 3.90e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.42e-05 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 1.42e-05 ) ; + Last LinSolve(iter,res) = ( 3, 7.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19708422.612369962 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20030112.90534688 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 19389038.640460264 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281852 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0581549 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.28903e+07s, dt:149699s, Cycle: 215 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 1.91e-08 ) ; ( R ) = ( 4.55e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.35e-02 ) ; ( Rwell ) = ( 6.10e-07 ) ; ( R ) = ( 7.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.89e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 2.86e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.43e-02 ) ; ( Rwell ) = ( 3.77e-07 ) ; ( R ) = ( 2.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.17e-05 ) ; ( Rwell ) = ( 1.20e-07 ) ; ( R ) = ( 4.17e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19774466.968264736 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20095654.72862429 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +wellControls3: BHP (at the specified reference elevation): 19455625.34731026 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.321156 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.069881 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.304e+07s, dt:149869s, Cycle: 216 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 1.21e-07 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.63e-02 ) ; ( Rwell ) = ( 8.66e-07 ) ; ( R ) = ( 7.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.42e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.18e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.17e-03 ) ; ( Rwell ) = ( 3.03e-07 ) ; ( R ) = ( 7.17e-03 ) ; + Last LinSolve(iter,res) = ( 6, 4.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.71e-05 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 8.71e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19840099.443055514 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 20160548.935479797 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 19521724.407489996 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.314164 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.124379 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.31899e+07s, dt:98734.8s, Cycle: 217 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.94e-02 ) ; ( Rwell ) = ( 3.14e-08 ) ; ( R ) = ( 4.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.78e-02 ) ; ( Rwell ) = ( 9.38e-07 ) ; ( R ) = ( 2.78e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.30e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.77e-04 ) ; ( Rwell ) = ( 2.17e-08 ) ; ( R ) = ( 4.77e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.29e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19883388.58241768 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20203182.711746313 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 19565370.31866251 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.212566 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753619 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.32886e+07s, dt:93937.8s, Cycle: 218 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.49e-02 ) ; ( Rwell ) = ( 2.17e-08 ) ; ( R ) = ( 4.49e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.05e-02 ) ; ( Rwell ) = ( 9.43e-07 ) ; ( R ) = ( 1.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.78e-05 ) ; ( Rwell ) = ( 1.74e-08 ) ; ( R ) = ( 7.78e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.63e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19924395.03604102 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20243578.011944935 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 19606719.857045762 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.198828 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588713 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.33826e+07s, dt:105074s, Cycle: 219 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 1.62e-08 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 2.99e-06 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.51e-04 ) ; ( Rwell ) = ( 2.22e-07 ) ; ( R ) = ( 4.51e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.76e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 19970684.56295377 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 20289243.89384724 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 19653297.378481038 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22296 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0581421 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.34877e+07s, dt:118451s, Cycle: 220 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.33e-02 ) ; ( Rwell ) = ( 2.23e-07 ) ; ( R ) = ( 4.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.02e-02 ) ; ( Rwell ) = ( 1.39e-06 ) ; ( R ) = ( 5.02e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.52e-02 ) ; ( Rwell ) = ( 7.25e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.16e-03 ) ; ( Rwell ) = ( 7.00e-07 ) ; ( R ) = ( 4.16e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.66e-05 ) ; ( Rwell ) = ( 1.00e-08 ) ; ( R ) = ( 1.66e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.60e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20022928.50132058 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 20340721.964891613 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 19705638.298381053 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254477 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672255 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.36061e+07s, dt:121666s, Cycle: 221 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.19e-02 ) ; ( Rwell ) = ( 9.19e-09 ) ; ( R ) = ( 4.19e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 1.10e-06 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 3.74e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.89e-05 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 4.89e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.64e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20075930.6674722 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 20392993.12304485 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 19758873.935660094 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.259967 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762417 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.37278e+07s, dt:114840s, Cycle: 222 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 4.74e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.04e-02 ) ; ( Rwell ) = ( 1.52e-06 ) ; ( R ) = ( 2.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.71e-04 ) ; ( Rwell ) = ( 2.69e-08 ) ; ( R ) = ( 5.71e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20125700.05589103 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20442054.52896284 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 19809025.03108489 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.24083 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684945 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.38426e+07s, dt:116510s, Cycle: 223 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.29e-02 ) ; ( Rwell ) = ( 2.79e-08 ) ; ( R ) = ( 4.29e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.66e-02 ) ; ( Rwell ) = ( 1.33e-06 ) ; ( R ) = ( 1.66e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.78e-05 ) ; ( Rwell ) = ( 2.19e-08 ) ; ( R ) = ( 2.78e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20175738.819198485 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 20491300.40883416 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 19859396.63476013 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.238192 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600446 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.39591e+07s, dt:128714s, Cycle: 224 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.21e-02 ) ; ( Rwell ) = ( 2.30e-08 ) ; ( R ) = ( 4.21e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.30e-02 ) ; ( Rwell ) = ( 2.22e-06 ) ; ( R ) = ( 6.30e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.60e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.72e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 5.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.01e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.85e-02 ) ; ( Rwell ) = ( 1.60e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.61e-02 ) ; ( Rwell ) = ( 5.02e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.91e-03 ) ; ( Rwell ) = ( 1.05e-06 ) ; ( R ) = ( 9.91e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.26e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.61e-04 ) ; ( Rwell ) = ( 5.49e-09 ) ; ( R ) = ( 1.61e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.04e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20231106.935732372 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 20545660.945997328 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 19914929.654497895 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.257823 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565796 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.40878e+07s, dt:147576s, Cycle: 225 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.23e-02 ) ; ( Rwell ) = ( 5.49e-09 ) ; ( R ) = ( 4.23e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.53e-02 ) ; ( Rwell ) = ( 4.63e-07 ) ; ( R ) = ( 1.53e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.87e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.46e-04 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 1.46e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20294801.759453155 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 20608608.724250738 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 19978884.12095094 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303942 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0739788 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.42354e+07s, dt:142188s, Cycle: 226 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 1.31e-07 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-01 ) ; ( Rwell ) = ( 4.32e-07 ) ; ( R ) = ( 1.23e-01 ) ; + Last LinSolve(iter,res) = ( 5, 4.90e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 2.81e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.04e-02 ) ; ( Rwell ) = ( 2.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.82e-05 ) ; ( Rwell ) = ( 6.43e-08 ) ; ( R ) = ( 4.82e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20356568.69642135 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 20669635.08542554 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20041016.14270786 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.303773 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0795795 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.43776e+07s, dt:130300s, Cycle: 227 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 6.58e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.93e-02 ) ; ( Rwell ) = ( 3.81e-06 ) ; ( R ) = ( 1.93e-02 ) ; + Last LinSolve(iter,res) = ( 4, 9.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.20e-04 ) ; ( Rwell ) = ( 1.69e-07 ) ; ( R ) = ( 1.20e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20413296.943946846 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 20725662.20047843 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 20098063.32844915 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281458 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0785239 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.45079e+07s, dt:120517s, Cycle: 228 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 1.70e-07 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.40e-02 ) ; ( Rwell ) = ( 2.37e-06 ) ; ( R ) = ( 2.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.84e-04 ) ; ( Rwell ) = ( 1.86e-08 ) ; ( R ) = ( 3.84e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.78e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20465354.40001312 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 20776918.878762122 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20150287.76876397 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254544 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0741736 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.46284e+07s, dt:115910s, Cycle: 229 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 2.02e-08 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.40e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 1.40e-02 ) ; + Last LinSolve(iter,res) = ( 4, 8.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.11e-04 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 8.11e-04 ) ; + Last LinSolve(iter,res) = ( 3, 9.77e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20514655.310026433 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 20825428.325418912 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20199739.845027987 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233953 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0683976 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.47443e+07s, dt:117706s, Cycle: 230 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.65e-02 ) ; ( Rwell ) = ( 1.57e-06 ) ; ( R ) = ( 6.65e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.82e-02 ) ; ( Rwell ) = ( 7.79e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.71e-03 ) ; ( Rwell ) = ( 7.38e-07 ) ; ( R ) = ( 5.71e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.08e-05 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 2.08e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.25e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20563982.95386813 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 20873972.377181333 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20249209.950081754 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.236216 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0620953 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.4862e+07s, dt:127289s, Cycle: 231 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.79e-08 ) ; ( R ) = ( 4.59e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.92e-02 ) ; ( Rwell ) = ( 2.06e-06 ) ; ( R ) = ( 7.92e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.94e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.15e-02 ) ; ( Rwell ) = ( 1.83e-06 ) ; ( R ) = ( 1.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.79e-05 ) ; ( Rwell ) = ( 7.89e-08 ) ; ( R ) = ( 4.79e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.97e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20617386.596230593 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 20926965.386034667 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 20303024.340250157 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260201 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0600539 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.49893e+07s, dt:140608s, Cycle: 232 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.63e-01 ) ; ( Rwell ) = ( 3.58e-06 ) ; ( R ) = ( 4.63e-01 ) ; + Last LinSolve(iter,res) = ( 5, 9.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-01 ) ; ( Rwell ) = ( 1.77e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.13e-01 ) ; ( Rwell ) = ( 8.60e-07 ) ; + Line search @ 0.125: ( Rflow ) = ( 6.42e-02 ) ; ( Rwell ) = ( 4.06e-07 ) ; + Line search @ 0.062: ( Rflow ) = ( 4.09e-02 ) ; ( Rwell ) = ( 1.79e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.45e-02 ) ; ( Rwell ) = ( 4.53e-07 ) ; ( R ) = ( 2.45e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.26e-04 ) ; ( Rwell ) = ( 2.10e-07 ) ; ( R ) = ( 5.26e-04 ) ; + Last LinSolve(iter,res) = ( 3, 7.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20676354.6918925 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 20985313.64037178 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20362257.532960534 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.283066 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0805362 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.51299e+07s, dt:127785s, Cycle: 233 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 2.10e-07 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.90e-02 ) ; ( Rwell ) = ( 1.06e-06 ) ; ( R ) = ( 1.90e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-03 ) ; ( Rwell ) = ( 1.19e-08 ) ; ( R ) = ( 5.10e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.75e-06 ) ; ( Rwell ) = ( 8.46e-09 ) ; ( R ) = ( 8.75e-06 ) ; + Last LinSolve(iter,res) = ( 3, 3.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20730142.755422816 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.000277318462702649 sm3/s +wellControls2: BHP (at the specified reference elevation): 21038498.771737054 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20416330.576158196 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.264861 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734401 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.52577e+07s, dt:123731s, Cycle: 234 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 9.96e-09 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.86e-02 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 2.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.20e-04 ) ; ( Rwell ) = ( 5.74e-09 ) ; ( R ) = ( 3.20e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.48e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20782174.751666956 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21089774.701739665 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20468435.261398416 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.256957 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682653 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.53815e+07s, dt:125810s, Cycle: 235 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 5.15e-09 ) ; ( R ) = ( 4.27e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.68e-02 ) ; ( Rwell ) = ( 1.03e-06 ) ; ( R ) = ( 3.68e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-02 ) ; ( Rwell ) = ( 9.27e-08 ) ; ( R ) = ( 1.02e-02 ) ; + Last LinSolve(iter,res) = ( 4, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.11e-05 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 5.11e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20835112.95254677 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 21141778.136546705 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 20521433.783338293 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.252212 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0661996 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.55073e+07s, dt:130534s, Cycle: 236 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.60e-08 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.31e-06 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 2.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.29e-04 ) ; ( Rwell ) = ( 2.62e-08 ) ; ( R ) = ( 5.29e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20889872.562139016 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 21195583.6408555 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 20576264.580820214 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.257098 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0601055 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.56378e+07s, dt:130205s, Cycle: 237 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.91e-02 ) ; ( Rwell ) = ( 2.46e-08 ) ; ( R ) = ( 3.91e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.94e-02 ) ; ( Rwell ) = ( 1.15e-06 ) ; ( R ) = ( 2.94e-02 ) ; + Last LinSolve(iter,res) = ( 6, 1.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.59e-04 ) ; ( Rwell ) = ( 1.48e-07 ) ; ( R ) = ( 3.59e-04 ) ; + Last LinSolve(iter,res) = ( 4, 6.95e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20943839.52919437 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 21248640.894672535 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 20630153.27084229 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.234905 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0667786 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.5768e+07s, dt:134326s, Cycle: 238 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.83e-02 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 3.83e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.15e-02 ) ; ( Rwell ) = ( 3.20e-06 ) ; ( R ) = ( 3.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.82e-03 ) ; ( Rwell ) = ( 3.66e-08 ) ; ( R ) = ( 3.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.72e-05 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 2.72e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 20999578.29185547 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21303491.2497427 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 20685878.53236884 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243578 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672371 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.59023e+07s, dt:137956s, Cycle: 239 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.92e-02 ) ; ( Rwell ) = ( 1.01e-08 ) ; ( R ) = ( 3.92e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.18e-02 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 2.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.62e-04 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 1.62e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21056512.70076125 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 21359663.262314547 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 20742857.117337834 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249047 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0740844 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.60403e+07s, dt:132791s, Cycle: 240 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.93e-02 ) ; ( Rwell ) = ( 3.62e-08 ) ; ( R ) = ( 3.93e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 8.32e-07 ) ; ( R ) = ( 3.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.61e-04 ) ; ( Rwell ) = ( 3.40e-08 ) ; ( R ) = ( 6.61e-04 ) ; + Last LinSolve(iter,res) = ( 5, 3.87e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21111167.56470688 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 21413393.615267936 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20797535.81985033 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.246279 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0766686 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.61731e+07s, dt:124861s, Cycle: 241 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.11e-02 ) ; ( Rwell ) = ( 3.25e-08 ) ; ( R ) = ( 4.11e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.81e-02 ) ; ( Rwell ) = ( 2.46e-06 ) ; ( R ) = ( 1.81e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.60e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.74e-03 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 5.74e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 4.85e-04 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 4.85e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21162987.61152248 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 21464373.548951793 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 20849468.108581036 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.233678 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0713214 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.62979e+07s, dt:123309s, Cycle: 242 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.15e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 4.15e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.14e-02 ) ; ( Rwell ) = ( 2.20e-06 ) ; ( R ) = ( 1.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-05 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 4.52e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21214390.815099917 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 21515220.53308164 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20901212.349526495 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243963 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0751318 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.64212e+07s, dt:117563s, Cycle: 243 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.57e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.11e-03 ) ; ( Rwell ) = ( 2.77e-07 ) ; ( R ) = ( 5.11e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-05 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 5.94e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.86e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21263766.115450047 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 21563572.181429956 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 20950629.055303182 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.22475 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769954 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.65388e+07s, dt:110220s, Cycle: 244 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-02 ) ; ( Rwell ) = ( 2.57e-07 ) ; ( R ) = ( 4.86e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.23e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.63e-03 ) ; ( Rwell ) = ( 1.79e-07 ) ; ( R ) = ( 3.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.22e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.09e-05 ) ; ( Rwell ) = ( 4.43e-09 ) ; ( R ) = ( 1.09e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21309868.617182717 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21608955.31437013 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 20996814.830421824 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.213421 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0675449 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.6649e+07s, dt:112859s, Cycle: 245 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.03e-02 ) ; ( Rwell ) = ( 5.82e-09 ) ; ( R ) = ( 4.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 3.83e-07 ) ; ( R ) = ( 3.97e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.22e-05 ) ; ( Rwell ) = ( 1.92e-08 ) ; ( R ) = ( 6.22e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21356630.837906357 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21654902.753383793 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21043653.415964115 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218918 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0672487 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.67619e+07s, dt:115896s, Cycle: 246 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.00e-02 ) ; ( Rwell ) = ( 7.23e-07 ) ; ( R ) = ( 9.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.14e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.55e-02 ) ; ( Rwell ) = ( 3.71e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.09e-02 ) ; ( Rwell ) = ( 1.95e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.97e-03 ) ; ( Rwell ) = ( 3.54e-07 ) ; ( R ) = ( 6.97e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.52e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.07e-05 ) ; ( Rwell ) = ( 2.73e-08 ) ; ( R ) = ( 3.07e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21404381.647704035 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 21701927.590603676 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 21091594.306725085 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.223599 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066836 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.68778e+07s, dt:119497s, Cycle: 247 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 2.73e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.39e-02 ) ; ( Rwell ) = ( 1.95e-06 ) ; ( R ) = ( 9.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.62e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 5.18e-02 ) ; ( Rwell ) = ( 9.88e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.27e-02 ) ; ( Rwell ) = ( 5.08e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-02 ) ; ( Rwell ) = ( 1.64e-06 ) ; ( R ) = ( 1.35e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.53e-05 ) ; ( Rwell ) = ( 1.29e-08 ) ; ( R ) = ( 7.53e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21453822.383788466 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 21750286.535045817 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 21141037.223105703 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218152 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0803157 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.69973e+07s, dt:108807s, Cycle: 248 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 1.15e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.71e-03 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 6.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.96e-05 ) ; ( Rwell ) = ( 9.63e-09 ) ; ( R ) = ( 7.96e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.90e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21498472.29299286 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 21794056.843867775 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21185722.17947041 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.201247 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762465 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.71061e+07s, dt:102697s, Cycle: 249 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 9.63e-09 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.27e-02 ) ; ( Rwell ) = ( 1.30e-06 ) ; ( R ) = ( 2.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.24e-04 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 2.24e-04 ) ; + Last LinSolve(iter,res) = ( 6, 6.16e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21540971.010483034 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21835818.649302453 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 21228223.33987763 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195099 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695607 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.72088e+07s, dt:103129s, Cycle: 250 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.07e-02 ) ; ( Rwell ) = ( 5.96e-09 ) ; ( R ) = ( 4.07e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.22e-06 ) ; ( R ) = ( 4.04e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.16e-04 ) ; ( Rwell ) = ( 7.58e-08 ) ; ( R ) = ( 1.16e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.70e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21583722.882155802 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21877868.74575062 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 21271027.16152917 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.195442 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626065 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.73119e+07s, dt:110941s, Cycle: 251 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 7.70e-08 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.23e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 1.23e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 5.16e-08 ) ; ( R ) = ( 1.54e-02 ) ; + Last LinSolve(iter,res) = ( 4, 6.16e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 6.72e-03 ) ; ( Rwell ) = ( 6.56e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.99e-05 ) ; ( Rwell ) = ( 2.75e-08 ) ; ( R ) = ( 1.99e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21629565.595507413 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 21922845.623042718 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21316887.326949526 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.206373 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0565933 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.74229e+07s, dt:127179s, Cycle: 252 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.99e-02 ) ; ( Rwell ) = ( 2.88e-08 ) ; ( R ) = ( 3.99e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.82e-02 ) ; ( Rwell ) = ( 2.27e-06 ) ; ( R ) = ( 1.82e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.82e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.03e-05 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.03e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.05e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21682007.040599212 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 21974355.05439386 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 21369394.636904005 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.231338 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612759 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.755e+07s, dt:138704s, Cycle: 253 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 1.12e-08 ) ; ( R ) = ( 3.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 2.42e-06 ) ; ( R ) = ( 4.16e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.55e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.20e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.67e-03 ) ; ( Rwell ) = ( 1.26e-06 ) ; ( R ) = ( 3.67e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.58e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-05 ) ; ( Rwell ) = ( 2.09e-08 ) ; ( R ) = ( 2.37e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21738870.091861606 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22030235.53303721 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 21426316.80989576 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.242689 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.068717 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.76887e+07s, dt:140419s, Cycle: 254 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 1.95e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.85e-03 ) ; ( Rwell ) = ( 2.30e-06 ) ; ( R ) = ( 9.85e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.03e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.89e-04 ) ; ( Rwell ) = ( 4.99e-08 ) ; ( R ) = ( 5.89e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21796264.582132213 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 22086705.732589103 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 21483767.53190609 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.242551 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0782659 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.78292e+07s, dt:130172s, Cycle: 255 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 5.10e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.58e-03 ) ; ( Rwell ) = ( 2.52e-06 ) ; ( R ) = ( 8.58e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.92e-03 ) ; ( Rwell ) = ( 1.38e-08 ) ; ( R ) = ( 1.92e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.28e-06 ) ; ( Rwell ) = ( 8.15e-09 ) ; ( R ) = ( 9.28e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21849529.580101226 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22138871.10106899 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 21537044.467591412 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.226308 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0665031 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.79593e+07s, dt:134657s, Cycle: 256 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.75e-02 ) ; ( Rwell ) = ( 8.15e-09 ) ; ( R ) = ( 3.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.30e-03 ) ; ( Rwell ) = ( 2.39e-07 ) ; ( R ) = ( 9.30e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.04e-03 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 1.04e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.34e-06 ) ; ( Rwell ) = ( 3.87e-09 ) ; ( R ) = ( 2.34e-06 ) ; + Last LinSolve(iter,res) = ( 3, 7.62e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21904109.86851281 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22192412.397868577 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 21591618.60946519 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.224289 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0578958 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8094e+07s, dt:152202s, Cycle: 257 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.65e-02 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 3.65e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.56e-02 ) ; ( Rwell ) = ( 8.97e-07 ) ; ( R ) = ( 2.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.07e-03 ) ; ( Rwell ) = ( 3.09e-08 ) ; ( R ) = ( 2.07e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.37e-06 ) ; ( Rwell ) = ( 2.68e-09 ) ; ( R ) = ( 2.37e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 21965925.460282806 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 22253216.733134568 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 21653449.05435523 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.256266 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0543877 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.82462e+07s, dt:178786s, Cycle: 258 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 2.45e-09 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 1.21e-06 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.27e-03 ) ; ( Rwell ) = ( 8.45e-08 ) ; ( R ) = ( 1.27e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.53e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.81e-07 ) ; ( Rwell ) = ( 3.75e-10 ) ; ( R ) = ( 5.81e-07 ) ; + Last LinSolve(iter,res) = ( 6, 1.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22039161.01556664 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 22325172.400548257 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 21726554.064316202 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.306681 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0846443 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.8425e+07s, dt:156903s, Cycle: 259 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.68e-09 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.20e-02 ) ; ( Rwell ) = ( 9.08e-07 ) ; ( R ) = ( 1.20e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.54e-04 ) ; ( Rwell ) = ( 5.81e-08 ) ; ( R ) = ( 2.54e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22103477.060700525 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22388307.912786923 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026233 sm3/s +wellControls3: BHP (at the specified reference elevation): 21790748.972521435 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.270534 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0822711 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.85819e+07s, dt:140484s, Cycle: 260 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.94e-02 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 3.94e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.63e-02 ) ; ( Rwell ) = ( 9.03e-07 ) ; ( R ) = ( 2.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.47e-03 ) ; ( Rwell ) = ( 1.27e-07 ) ; ( R ) = ( 2.47e-03 ) ; + Last LinSolve(iter,res) = ( 4, 6.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.46e-06 ) ; ( Rwell ) = ( 5.19e-09 ) ; ( R ) = ( 2.46e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22160662.792533003 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22444583.821067393 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 21847828.152389187 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.236317 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0753746 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 1.87224e+07s, dt:133644s, Cycle: 261 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.97e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 3.97e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 8.72e-07 ) ; ( R ) = ( 4.36e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.96e-02 ) ; ( Rwell ) = ( 4.35e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.99e-03 ) ; ( Rwell ) = ( 4.58e-07 ) ; ( R ) = ( 4.99e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.01e-06 ) ; ( Rwell ) = ( 2.34e-08 ) ; ( R ) = ( 8.01e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.65e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22214558.349627066 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22497516.27931259 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 21901561.863619767 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.225488 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688334 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.8856e+07s, dt:135145s, Cycle: 262 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 2.26e-08 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.43e-02 ) ; ( Rwell ) = ( 1.21e-06 ) ; ( R ) = ( 3.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.10e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.21e-03 ) ; ( Rwell ) = ( 1.71e-08 ) ; ( R ) = ( 3.21e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.24e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.30e-06 ) ; ( Rwell ) = ( 1.63e-09 ) ; ( R ) = ( 6.30e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.01e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22269311.249822434 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22551109.905369833 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 21956112.014812134 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.230676 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623024 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.89911e+07s, dt:145837s, Cycle: 263 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 1.77e-09 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.56e-02 ) ; ( Rwell ) = ( 1.64e-06 ) ; ( R ) = ( 1.56e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.71e-03 ) ; ( Rwell ) = ( 6.12e-08 ) ; ( R ) = ( 1.71e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.77e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.06e-05 ) ; ( Rwell ) = ( 2.27e-09 ) ; ( R ) = ( 1.06e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.20e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22328661.46402825 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 22609495.072320726 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 22015410.13753575 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0662131 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.9137e+07s, dt:151293s, Cycle: 264 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.45e-09 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 5.06e-07 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.46e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.96e-05 ) ; ( Rwell ) = ( 8.14e-08 ) ; ( R ) = ( 7.96e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22390429.61198555 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 22670140.013636433 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 22077200.38219628 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254495 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.067224 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.92883e+07s, dt:155402s, Cycle: 265 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 8.24e-08 ) ; ( R ) = ( 3.63e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.87e-02 ) ; ( Rwell ) = ( 6.65e-07 ) ; ( R ) = ( 9.87e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.80e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.63e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.00e-02 ) ; ( Rwell ) = ( 1.19e-07 ) ; ( R ) = ( 1.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 3.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.12e-05 ) ; ( Rwell ) = ( 2.33e-08 ) ; ( R ) = ( 3.12e-05 ) ; + Last LinSolve(iter,res) = ( 4, 3.74e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22454123.23937908 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 22732601.448207352 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 22140918.652570743 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265666 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.266629 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0616677 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.94437e+07s, dt:168797s, Cycle: 266 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.67e-02 ) ; ( Rwell ) = ( 2.45e-08 ) ; ( R ) = ( 3.67e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 1.66e-06 ) ; ( R ) = ( 4.26e-02 ) ; + Last LinSolve(iter,res) = ( 6, 8.77e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.80e-02 ) ; ( Rwell ) = ( 8.29e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.87e-03 ) ; ( Rwell ) = ( 9.98e-07 ) ; ( R ) = ( 6.87e-03 ) ; + Last LinSolve(iter,res) = ( 6, 8.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.07e-05 ) ; ( Rwell ) = ( 4.89e-08 ) ; ( R ) = ( 5.07e-05 ) ; + Last LinSolve(iter,res) = ( 3, 8.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22522673.9499703 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 22799889.816377126 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 22209376.448748637 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.297387 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0689835 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.96125e+07s, dt:170447s, Cycle: 267 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.89e-02 ) ; ( Rwell ) = ( 5.00e-08 ) ; ( R ) = ( 3.89e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.24e-02 ) ; ( Rwell ) = ( 2.00e-06 ) ; ( R ) = ( 5.24e-02 ) ; + Last LinSolve(iter,res) = ( 6, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 1.00e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-02 ) ; ( Rwell ) = ( 7.14e-07 ) ; ( R ) = ( 4.52e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.92e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.07e-02 ) ; ( Rwell ) = ( 8.58e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 1.45e-02 ) ; ( Rwell ) = ( 9.30e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.74e-03 ) ; ( Rwell ) = ( 5.29e-07 ) ; ( R ) = ( 1.74e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 2.51e-06 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 2.51e-06 ) ; + Last LinSolve(iter,res) = ( 5, 4.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22591675.391449124 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 22867477.504578207 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 22278199.171062484 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.306863 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0682279 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.97829e+07s, dt:173373s, Cycle: 268 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 6.08e-09 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.00e-02 ) ; ( Rwell ) = ( 8.64e-07 ) ; ( R ) = ( 3.00e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.64e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 9.02e-08 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 3.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22661517.61787745 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 22936098.328853052 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 22347973.075987082 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.305347 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.066993 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 1.99563e+07s, dt:178484s, Cycle: 269 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 9.11e-08 ) ; ( R ) = ( 4.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.27e-02 ) ; ( Rwell ) = ( 8.98e-07 ) ; ( R ) = ( 1.27e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.25e-03 ) ; ( Rwell ) = ( 5.88e-08 ) ; ( R ) = ( 1.25e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.42e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.10e-06 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 3.10e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22733081.97068935 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 23006380.113934465 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 22419395.47020832 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.298793 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0742321 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.01348e+07s, dt:171569s, Cycle: 270 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.00e-02 ) ; ( Rwell ) = ( 3.71e-09 ) ; ( R ) = ( 4.00e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.62e-02 ) ; ( Rwell ) = ( 8.99e-07 ) ; ( R ) = ( 6.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.47e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.96e-02 ) ; ( Rwell ) = ( 4.50e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 4.42e-07 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.32e-05 ) ; ( Rwell ) = ( 5.78e-08 ) ; ( R ) = ( 9.32e-05 ) ; + Last LinSolve(iter,res) = ( 3, 9.45e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22801519.024395097 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 23073614.80905719 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 22487725.84254246 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.294208 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0784129 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.03063e+07s, dt:158842s, Cycle: 271 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.28e-02 ) ; ( Rwell ) = ( 5.84e-08 ) ; ( R ) = ( 4.28e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.15e-02 ) ; ( Rwell ) = ( 1.82e-06 ) ; ( R ) = ( 7.15e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.60e-02 ) ; ( Rwell ) = ( 9.06e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.64e-03 ) ; ( Rwell ) = ( 9.64e-07 ) ; ( R ) = ( 4.64e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.25e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.49e-04 ) ; ( Rwell ) = ( 1.36e-08 ) ; ( R ) = ( 3.49e-04 ) ; + Last LinSolve(iter,res) = ( 6, 5.31e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22865160.460247237 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 23135954.120645467 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 22551301.685022276 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281459 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0691796 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.04652e+07s, dt:160093s, Cycle: 272 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.43e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.35e-02 ) ; ( Rwell ) = ( 1.31e-06 ) ; ( R ) = ( 3.35e-02 ) ; + Last LinSolve(iter,res) = ( 6, 4.83e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.83e-04 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 4.83e-04 ) ; + Last LinSolve(iter,res) = ( 4, 5.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 22929637.559764873 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 23199167.981954303 Pa +wellControls2: Total rate: 56.328373541922936 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026258 sm3/s +wellControls3: BHP (at the specified reference elevation): 22615701.44628298 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026284 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.278249 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0575491 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.06253e+07s, dt:181631s, Cycle: 273 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.17e-02 ) ; ( Rwell ) = ( 3.00e-07 ) ; ( R ) = ( 4.17e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.44e-02 ) ; ( Rwell ) = ( 2.35e-06 ) ; ( R ) = ( 2.44e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.27e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.60e-03 ) ; ( Rwell ) = ( 7.55e-08 ) ; ( R ) = ( 2.60e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.66e-06 ) ; ( Rwell ) = ( 5.11e-09 ) ; ( R ) = ( 5.66e-06 ) ; + Last LinSolve(iter,res) = ( 4, 4.72e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23003412.68185511 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 23271494.946664184 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 22689379.056866232 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.281702 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641397 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.08069e+07s, dt:192367s, Cycle: 274 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.52e-02 ) ; ( Rwell ) = ( 4.40e-09 ) ; ( R ) = ( 3.52e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.64e-02 ) ; ( Rwell ) = ( 1.46e-06 ) ; ( R ) = ( 3.64e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.31e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.58e-02 ) ; ( Rwell ) = ( 7.27e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.35e-03 ) ; ( Rwell ) = ( 6.75e-07 ) ; ( R ) = ( 3.35e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.67e-04 ) ; ( Rwell ) = ( 1.69e-08 ) ; ( R ) = ( 3.67e-04 ) ; + Last LinSolve(iter,res) = ( 5, 6.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23081429.37223441 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 23348154.576610062 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 22767276.519564193 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.301915 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0759639 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.09993e+07s, dt:182028s, Cycle: 275 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.76e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.61e-02 ) ; ( Rwell ) = ( 1.67e-06 ) ; ( R ) = ( 3.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.16e-04 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 5.16e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.40e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23154833.71199422 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 23420122.044918466 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 22840531.388242908 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.290129 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0746577 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.11813e+07s, dt:174297s, Cycle: 276 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.06e-02 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 4.06e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.83e-02 ) ; ( Rwell ) = ( 1.49e-06 ) ; ( R ) = ( 1.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.36e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.27e-04 ) ; ( Rwell ) = ( 3.54e-08 ) ; ( R ) = ( 2.27e-04 ) ; + Last LinSolve(iter,res) = ( 5, 7.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23224766.968730766 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 23488720.328664377 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 22910335.394779973 Pa +wellControls3: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026643 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.283125 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0695815 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.13556e+07s, dt:174994s, Cycle: 277 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 3.64e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.99e-02 ) ; ( Rwell ) = ( 1.37e-06 ) ; ( R ) = ( 1.99e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.56e-04 ) ; ( Rwell ) = ( 3.63e-08 ) ; ( R ) = ( 1.56e-04 ) ; + Last LinSolve(iter,res) = ( 5, 8.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23294989.388284676 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 23557541.17590537 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 22980400.127277236 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.290119 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0639376 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.15306e+07s, dt:185717s, Cycle: 278 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.72e-02 ) ; ( Rwell ) = ( 1.91e-06 ) ; ( R ) = ( 2.72e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.57e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 8.47e-08 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.53e-06 ) ; ( Rwell ) = ( 2.94e-09 ) ; ( R ) = ( 1.53e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.79e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23369865.448512975 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 23631075.061333522 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23055173.045771215 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.310245 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0679098 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.17163e+07s, dt:189489s, Cycle: 279 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.73e-02 ) ; ( Rwell ) = ( 3.97e-09 ) ; ( R ) = ( 3.73e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-02 ) ; ( Rwell ) = ( 1.72e-06 ) ; ( R ) = ( 1.49e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.79e-05 ) ; ( Rwell ) = ( 1.34e-08 ) ; ( R ) = ( 6.79e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.18e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23446179.4808966 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 23706066.466195133 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 23131378.484341513 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.30819 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0715947 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.19058e+07s, dt:186654s, Cycle: 280 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.86e-02 ) ; ( Rwell ) = ( 1.44e-08 ) ; ( R ) = ( 3.86e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.24e-02 ) ; ( Rwell ) = ( 1.46e-06 ) ; ( R ) = ( 3.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.67e-05 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 7.67e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.19e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23521346.84692883 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 23779852.45856758 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 23206436.841334134 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.291839 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0654538 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.20925e+07s, dt:195101s, Cycle: 281 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 1.90e-08 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 1.99e-06 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.35e-04 ) ; ( Rwell ) = ( 3.83e-08 ) ; ( R ) = ( 8.35e-04 ) ; + Last LinSolve(iter,res) = ( 5, 4.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23599867.901919246 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 23856878.626453966 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 23284854.26154114 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.296182 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0623441 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.22876e+07s, dt:210446s, Cycle: 282 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 3.92e-08 ) ; ( R ) = ( 3.84e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.61e-02 ) ; ( Rwell ) = ( 2.37e-06 ) ; ( R ) = ( 2.61e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.92e-04 ) ; ( Rwell ) = ( 5.13e-08 ) ; ( R ) = ( 5.92e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23684336.240832593 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 23939740.68955859 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23369250.63001859 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.322012 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0588384 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.2498e+07s, dt:235477s, Cycle: 283 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.98e-02 ) ; ( Rwell ) = ( 5.18e-08 ) ; ( R ) = ( 3.98e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.84e-02 ) ; ( Rwell ) = ( 2.40e-06 ) ; ( R ) = ( 2.84e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.14e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.23e-04 ) ; ( Rwell ) = ( 9.42e-08 ) ; ( R ) = ( 2.23e-04 ) ; + Last LinSolve(iter,res) = ( 5, 9.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23778605.830452695 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 24032330.363923945 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 23463422.0438841 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.362643 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.074912 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.27335e+07s, dt:224953s, Cycle: 284 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.88e-02 ) ; ( Rwell ) = ( 9.33e-08 ) ; ( R ) = ( 3.88e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 3.44e-06 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.15e-05 ) ; ( Rwell ) = ( 5.87e-08 ) ; ( R ) = ( 7.15e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.07e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23868915.800627496 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 24120866.20360878 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23553517.30298772 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.346472 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0728828 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.29584e+07s, dt:218942s, Cycle: 285 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.08e-02 ) ; ( Rwell ) = ( 5.79e-08 ) ; ( R ) = ( 4.08e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.19e-02 ) ; ( Rwell ) = ( 3.21e-06 ) ; ( R ) = ( 3.19e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.61e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.37e-05 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 9.37e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.53e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 23956482.030712854 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 24206888.16226381 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 23640923.63023805 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.327945 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734887 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.31774e+07s, dt:211902s, Cycle: 286 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.15e-07 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.13e-02 ) ; ( Rwell ) = ( 3.12e-06 ) ; ( R ) = ( 8.13e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.68e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.05e-02 ) ; ( Rwell ) = ( 1.57e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.28e-03 ) ; ( Rwell ) = ( 1.69e-06 ) ; ( R ) = ( 7.28e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.52e-05 ) ; ( Rwell ) = ( 1.52e-08 ) ; ( R ) = ( 1.52e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.80e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24041381.82761936 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 24290225.366899185 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls3: BHP (at the specified reference elevation): 23725816.487186663 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.325697 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0658704 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.33893e+07s, dt:220577s, Cycle: 287 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.18e-02 ) ; ( Rwell ) = ( 1.61e-08 ) ; ( R ) = ( 4.18e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-02 ) ; ( Rwell ) = ( 3.30e-06 ) ; ( R ) = ( 2.57e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.81e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-04 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 2.63e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.51e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24129618.816039428 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 24376855.341496397 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 23813968.095953505 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.343046 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0819526 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.36099e+07s, dt:198034s, Cycle: 288 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 1.32e-07 ) ; ( R ) = ( 4.05e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.00e-02 ) ; ( Rwell ) = ( 1.01e-06 ) ; ( R ) = ( 8.00e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.41e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 4.62e-07 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.41e-02 ) ; ( Rwell ) = ( 2.90e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.63e-02 ) ; ( Rwell ) = ( 7.58e-07 ) ; ( R ) = ( 1.63e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.16e-05 ) ; ( Rwell ) = ( 7.67e-08 ) ; ( R ) = ( 7.16e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24208571.131074257 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 24454456.551856846 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 23892872.820454773 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.292021 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0834699 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.38079e+07s, dt:175518s, Cycle: 289 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 7.75e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 1.66e-06 ) ; ( R ) = ( 5.03e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.35e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.13e-02 ) ; ( Rwell ) = ( 8.56e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.39e-03 ) ; ( Rwell ) = ( 1.01e-06 ) ; ( R ) = ( 4.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.54e-05 ) ; ( Rwell ) = ( 4.48e-09 ) ; ( R ) = ( 2.54e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24278283.530943953 Pa +wellControls1: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls2: BHP (at the specified reference elevation): 24522890.91413548 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 23962468.07770354 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.260774 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.076767 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.39834e+07s, dt:164891s, Cycle: 290 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.34e-02 ) ; ( Rwell ) = ( 5.38e-09 ) ; ( R ) = ( 4.34e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.08e-02 ) ; ( Rwell ) = ( 1.79e-06 ) ; ( R ) = ( 1.08e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.78e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.54e-05 ) ; ( Rwell ) = ( 8.02e-09 ) ; ( R ) = ( 4.54e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.83e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24343756.95501032 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 24587290.789483752 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +wellControls3: BHP (at the specified reference elevation): 24027876.331143245 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.249158 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0697904 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.41483e+07s, dt:165221s, Cycle: 291 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.38e-02 ) ; ( Rwell ) = ( 8.02e-09 ) ; ( R ) = ( 4.38e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.93e-06 ) ; ( R ) = ( 2.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.21e-03 ) ; ( Rwell ) = ( 3.76e-08 ) ; ( R ) = ( 2.21e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.97e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.94e-06 ) ; ( Rwell ) = ( 3.30e-09 ) ; ( R ) = ( 2.94e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.49e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24409753.72290651 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 24652198.144896768 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 24093918.80850075 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265915 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255659 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0630505 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.43135e+07s, dt:176931s, Cycle: 292 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 4.20e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.84e-02 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 3.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.35e-04 ) ; ( Rwell ) = ( 1.25e-07 ) ; ( R ) = ( 1.35e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24480228.36544884 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 24721489.219652306 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 24164382.03190127 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 29.999999999999993 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026386 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.274299 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0612228 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.44905e+07s, dt:193070s, Cycle: 293 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 1.26e-07 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.11e-01 ) ; ( Rwell ) = ( 2.22e-06 ) ; ( R ) = ( 1.11e-01 ) ; + Last LinSolve(iter,res) = ( 5, 7.61e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.95e-02 ) ; ( Rwell ) = ( 1.11e-06 ) ; + Line search @ 0.250: ( Rflow ) = ( 3.11e-02 ) ; ( Rwell ) = ( 5.55e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 1.60e-06 ) ; ( R ) = ( 4.22e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.05e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 1.54e-02 ) ; ( Rwell ) = ( 1.08e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.00e-03 ) ; ( Rwell ) = ( 8.84e-07 ) ; ( R ) = ( 5.00e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.73e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.78e-05 ) ; ( Rwell ) = ( 4.67e-09 ) ; ( R ) = ( 1.78e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24556701.59796472 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 24796535.32743928 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 24240679.999209322 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.280453 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0657923 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.46835e+07s, dt:201130s, Cycle: 294 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.35e-02 ) ; ( Rwell ) = ( 5.22e-09 ) ; ( R ) = ( 4.35e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.74e-02 ) ; ( Rwell ) = ( 2.20e-06 ) ; ( R ) = ( 1.74e-02 ) ; + Last LinSolve(iter,res) = ( 6, 5.21e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.01e-03 ) ; ( Rwell ) = ( 1.21e-07 ) ; ( R ) = ( 1.01e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.03e-06 ) ; ( Rwell ) = ( 1.45e-09 ) ; ( R ) = ( 2.03e-06 ) ; + Last LinSolve(iter,res) = ( 5, 2.19e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24636041.15541591 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 24874522.55095674 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 24319905.47843412 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.288183 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0637061 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.48847e+07s, dt:213955s, Cycle: 295 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 1.20e-09 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.59e-02 ) ; ( Rwell ) = ( 2.51e-06 ) ; ( R ) = ( 3.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.54e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.90e-03 ) ; ( Rwell ) = ( 1.74e-07 ) ; ( R ) = ( 1.90e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.45e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.72e-06 ) ; ( Rwell ) = ( 2.22e-09 ) ; ( R ) = ( 5.72e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.36e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24720722.748516906 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 24957793.305605166 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 24404504.231086858 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.308093 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0641457 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.50986e+07s, dt:226588s, Cycle: 296 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.36e-02 ) ; ( Rwell ) = ( 2.77e-09 ) ; ( R ) = ( 4.36e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.59e-02 ) ; ( Rwell ) = ( 2.52e-06 ) ; ( R ) = ( 7.59e-02 ) ; + Last LinSolve(iter,res) = ( 6, 6.87e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.17e-02 ) ; ( Rwell ) = ( 1.26e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.65e-03 ) ; ( Rwell ) = ( 1.17e-06 ) ; ( R ) = ( 6.65e-03 ) ; + Last LinSolve(iter,res) = ( 6, 7.17e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 3.73e-05 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 3.73e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.93e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24810511.913981445 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 25045955.867117595 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 24494173.83801988 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.328069 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0755754 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.53252e+07s, dt:215164s, Cycle: 297 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.13e-02 ) ; ( Rwell ) = ( 4.15e-08 ) ; ( R ) = ( 4.13e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.49e-01 ) ; ( Rwell ) = ( 1.88e-06 ) ; ( R ) = ( 1.49e-01 ) ; + Last LinSolve(iter,res) = ( 6, 5.75e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.01e-02 ) ; ( Rwell ) = ( 9.58e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 9.36e-07 ) ; ( R ) = ( 8.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 5.33e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.61e-05 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 1.61e-05 ) ; + Last LinSolve(iter,res) = ( 5, 8.02e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 24895397.972284768 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 25129421.350241795 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 24578968.505436193 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.307574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0762618 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.55404e+07s, dt:203054s, Cycle: 298 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.10e-08 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.05e-02 ) ; ( Rwell ) = ( 2.58e-06 ) ; ( R ) = ( 4.05e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.31e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.61e-03 ) ; ( Rwell ) = ( 1.16e-07 ) ; ( R ) = ( 1.61e-03 ) ; + Last LinSolve(iter,res) = ( 3, 6.79e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.01e-06 ) ; ( Rwell ) = ( 6.83e-10 ) ; ( R ) = ( 1.01e-06 ) ; + Last LinSolve(iter,res) = ( 7, 5.36e-04 ) ; +wellControls1: BHP (at the specified reference elevation): 24974866.863420922 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls2: BHP (at the specified reference elevation): 25207598.952093378 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 24658346.974658012 Pa +wellControls3: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279768 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0729699 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.57434e+07s, dt:197469s, Cycle: 299 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.15e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.24e-02 ) ; ( Rwell ) = ( 2.47e-06 ) ; ( R ) = ( 1.24e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.50e-03 ) ; ( Rwell ) = ( 8.90e-08 ) ; ( R ) = ( 2.50e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.87e-04 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 1.87e-04 ) ; + Last LinSolve(iter,res) = ( 3, 8.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25051900.198813986 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 25283359.404524088 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls3: BHP (at the specified reference elevation): 24735304.21145166 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.276684 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0688348 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.59409e+07s, dt:199685s, Cycle: 300 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 1.21e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.48e-02 ) ; ( Rwell ) = ( 2.25e-06 ) ; ( R ) = ( 1.48e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.14e-04 ) ; ( Rwell ) = ( 8.70e-08 ) ; ( R ) = ( 1.14e-04 ) ; + Last LinSolve(iter,res) = ( 4, 9.85e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25129746.89184453 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 25360006.348698605 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 24813103.108245265 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.285204 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0729207 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.61406e+07s, dt:194280s, Cycle: 301 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.14e-02 ) ; ( Rwell ) = ( 8.77e-08 ) ; ( R ) = ( 4.14e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.30e-02 ) ; ( Rwell ) = ( 2.14e-06 ) ; ( R ) = ( 2.30e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.25e-03 ) ; ( Rwell ) = ( 7.80e-08 ) ; ( R ) = ( 2.25e-03 ) ; + Last LinSolve(iter,res) = ( 4, 7.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.16e-06 ) ; ( Rwell ) = ( 8.13e-09 ) ; ( R ) = ( 6.16e-06 ) ; + Last LinSolve(iter,res) = ( 4, 7.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25205300.059666596 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026566 sm3/s +wellControls2: BHP (at the specified reference elevation): 25434407.105860915 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 24888601.73918165 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.272574 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0734365 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.63348e+07s, dt:188123s, Cycle: 302 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.16e-02 ) ; ( Rwell ) = ( 8.92e-09 ) ; ( R ) = ( 4.16e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.29e-02 ) ; ( Rwell ) = ( 8.51e-07 ) ; ( R ) = ( 2.29e-02 ) ; + Last LinSolve(iter,res) = ( 6, 9.65e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.52e-04 ) ; ( Rwell ) = ( 1.47e-07 ) ; ( R ) = ( 4.52e-04 ) ; + Last LinSolve(iter,res) = ( 4, 1.00e-02 ) ; +wellControls1: BHP (at the specified reference elevation): 25278700.59993593 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 25506588.37425939 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 24961963.03076382 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.255583 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0636535 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.6523e+07s, dt:200226s, Cycle: 303 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.10e-02 ) ; ( Rwell ) = ( 1.47e-07 ) ; ( R ) = ( 4.10e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.47e-02 ) ; ( Rwell ) = ( 2.46e-06 ) ; ( R ) = ( 1.47e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.63e-03 ) ; ( Rwell ) = ( 7.59e-08 ) ; ( R ) = ( 2.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.01e-06 ) ; ( Rwell ) = ( 4.53e-09 ) ; ( R ) = ( 8.01e-06 ) ; + Last LinSolve(iter,res) = ( 3, 7.10e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25357193.60404824 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 25583699.11003776 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 25040366.90709874 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.273639 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0616258 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.67232e+07s, dt:217578s, Cycle: 304 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 3.90e-02 ) ; ( Rwell ) = ( 5.32e-09 ) ; ( R ) = ( 3.90e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.28e-02 ) ; ( Rwell ) = ( 3.25e-06 ) ; ( R ) = ( 2.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.34e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.30e-04 ) ; ( Rwell ) = ( 5.98e-08 ) ; ( R ) = ( 7.30e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.41e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25442643.655040745 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls2: BHP (at the specified reference elevation): 25667783.859353952 Pa +wellControls2: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls3: BHP (at the specified reference elevation): 25125765.282820147 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.299859 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0768044 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.69408e+07s, dt:204337s, Cycle: 305 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.26e-02 ) ; ( Rwell ) = ( 6.05e-08 ) ; ( R ) = ( 4.26e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.95e-02 ) ; ( Rwell ) = ( 1.59e-06 ) ; ( R ) = ( 1.95e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.88e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.59e-03 ) ; ( Rwell ) = ( 4.07e-08 ) ; ( R ) = ( 1.59e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.37e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 5.96e-06 ) ; ( Rwell ) = ( 1.85e-09 ) ; ( R ) = ( 5.96e-06 ) ; + Last LinSolve(iter,res) = ( 4, 3.55e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25522764.06052871 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 25746720.065137804 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 25205847.758921195 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.279364 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.075817 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.71451e+07s, dt:193611s, Cycle: 306 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 1.85e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.59e-02 ) ; ( Rwell ) = ( 1.86e-06 ) ; ( R ) = ( 4.59e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.86e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.20e-02 ) ; ( Rwell ) = ( 9.31e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.44e-03 ) ; ( Rwell ) = ( 3.25e-07 ) ; ( R ) = ( 8.44e-03 ) ; + Last LinSolve(iter,res) = ( 6, 6.91e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.43e-05 ) ; ( Rwell ) = ( 4.69e-08 ) ; ( R ) = ( 6.43e-05 ) ; + Last LinSolve(iter,res) = ( 4, 8.26e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25598733.546596408 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 25821528.660724163 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 25281782.62760894 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.267724 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0763165 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.73387e+07s, dt:182624s, Cycle: 307 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.73e-08 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.14e-02 ) ; ( Rwell ) = ( 1.63e-06 ) ; ( R ) = ( 2.14e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.37e-05 ) ; ( Rwell ) = ( 2.21e-08 ) ; ( R ) = ( 3.37e-05 ) ; + Last LinSolve(iter,res) = ( 6, 4.50e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25670465.138156008 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls2: BHP (at the specified reference elevation): 25892038.824314874 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 25353441.033419907 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.254414 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0721886 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.75213e+07s, dt:178896s, Cycle: 308 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.47e-02 ) ; ( Rwell ) = ( 2.16e-08 ) ; ( R ) = ( 4.47e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.43e-02 ) ; ( Rwell ) = ( 1.50e-06 ) ; ( R ) = ( 1.43e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.99e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.65e-05 ) ; ( Rwell ) = ( 3.69e-08 ) ; ( R ) = ( 4.65e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.92e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25740499.131639197 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 25960897.257830024 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 25423397.071510762 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.250109 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0744067 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.77002e+07s, dt:171690s, Cycle: 309 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.20e-02 ) ; ( Rwell ) = ( 3.73e-08 ) ; ( R ) = ( 4.20e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.44e-02 ) ; ( Rwell ) = ( 8.61e-07 ) ; ( R ) = ( 1.44e-02 ) ; + Last LinSolve(iter,res) = ( 5, 9.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 7.36e-05 ) ; ( Rwell ) = ( 3.72e-08 ) ; ( R ) = ( 7.36e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25807813.060194273 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 26027140.514475442 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 25490716.422508862 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.24007 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0798144 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.78719e+07s, dt:157014s, Cycle: 310 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 3.72e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.83e-02 ) ; ( Rwell ) = ( 1.99e-06 ) ; ( R ) = ( 8.83e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.93e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 4.27e-02 ) ; ( Rwell ) = ( 1.02e-06 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.96e-03 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 5.96e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 6.04e-05 ) ; ( Rwell ) = ( 5.13e-08 ) ; ( R ) = ( 6.04e-05 ) ; + Last LinSolve(iter,res) = ( 4, 9.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25869427.674094472 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls2: BHP (at the specified reference elevation): 26087720.53402325 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +wellControls3: BHP (at the specified reference elevation): 25552349.276324 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.216735 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0743325 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.80289e+07s, dt:150792s, Cycle: 311 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.53e-02 ) ; ( Rwell ) = ( 5.19e-08 ) ; ( R ) = ( 4.53e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.98e-03 ) ; ( Rwell ) = ( 2.00e-06 ) ; ( R ) = ( 4.98e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.06e-04 ) ; ( Rwell ) = ( 7.77e-09 ) ; ( R ) = ( 8.06e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.54e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25928400.994996503 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26145655.620013602 Pa +wellControls2: Total rate: 56.32837354192293 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270262066 sm3/s +wellControls3: BHP (at the specified reference elevation): 25611242.947819926 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.203705 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0626428 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.81797e+07s, dt:162154s, Cycle: 312 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.42e-02 ) ; ( Rwell ) = ( 7.00e-09 ) ; ( R ) = ( 4.42e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.60e-02 ) ; ( Rwell ) = ( 2.12e-06 ) ; ( R ) = ( 2.60e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.59e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.73e-05 ) ; ( Rwell ) = ( 1.07e-07 ) ; ( R ) = ( 8.73e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.69e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 25991512.82743911 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 26207790.02591913 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 25674303.39153525 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.218328 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0594739 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.83419e+07s, dt:180220s, Cycle: 313 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 1.08e-07 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.06e-02 ) ; ( Rwell ) = ( 1.19e-06 ) ; ( R ) = ( 2.06e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.70e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.33e-03 ) ; ( Rwell ) = ( 9.42e-09 ) ; ( R ) = ( 1.33e-03 ) ; + Last LinSolve(iter,res) = ( 5, 6.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 2.23e-06 ) ; ( Rwell ) = ( 4.32e-10 ) ; ( R ) = ( 2.23e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.47e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26061314.64225273 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26276551.251257308 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 25744059.325136885 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.243025 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684205 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.85221e+07s, dt:182973s, Cycle: 314 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.22e-02 ) ; ( Rwell ) = ( 1.02e-09 ) ; ( R ) = ( 4.22e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.39e-02 ) ; ( Rwell ) = ( 1.14e-06 ) ; ( R ) = ( 1.39e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.86e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 2.80e-08 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.13e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.63e-06 ) ; ( Rwell ) = ( 7.25e-09 ) ; ( R ) = ( 9.63e-06 ) ; + Last LinSolve(iter,res) = ( 2, 9.66e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26132039.86237541 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 26346269.40526798 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 25814735.14317776 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.247227 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0569878 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.87051e+07s, dt:208855s, Cycle: 315 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 7.96e-09 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.87e-02 ) ; ( Rwell ) = ( 1.32e-06 ) ; ( R ) = ( 6.87e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.97e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 3.06e-02 ) ; ( Rwell ) = ( 6.62e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.39e-03 ) ; ( Rwell ) = ( 8.67e-07 ) ; ( R ) = ( 3.39e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.20e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 9.11e-06 ) ; ( Rwell ) = ( 1.30e-09 ) ; ( R ) = ( 9.11e-06 ) ; + Last LinSolve(iter,res) = ( 5, 3.14e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26213095.335310362 Pa +wellControls1: Total rate: 56.32837354192294 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026335 sm3/s +wellControls2: BHP (at the specified reference elevation): 26426115.020685732 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30.000000000000007 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537307 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263356 sm3/s +wellControls3: BHP (at the specified reference elevation): 25895724.12480854 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.282822 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.117539 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.89139e+07s, dt:143765s, Cycle: 316 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.77e-02 ) ; ( Rwell ) = ( 1.47e-09 ) ; ( R ) = ( 4.77e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.84e-02 ) ; ( Rwell ) = ( 3.07e-07 ) ; ( R ) = ( 4.84e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.57e-03 ) ; + Line search @ 0.500: ( Rflow ) = ( 2.39e-02 ) ; ( Rwell ) = ( 1.54e-07 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.95e-03 ) ; ( Rwell ) = ( 1.50e-07 ) ; ( R ) = ( 2.95e-03 ) ; + Last LinSolve(iter,res) = ( 5, 7.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.64e-06 ) ; ( Rwell ) = ( 3.22e-09 ) ; ( R ) = ( 8.64e-06 ) ; + Last LinSolve(iter,res) = ( 5, 8.22e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26268835.476059105 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 26481025.2174237 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls3: BHP (at the specified reference elevation): 25951446.174146563 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.187049 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0905749 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.90577e+07s, dt:120210s, Cycle: 317 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.66e-02 ) ; ( Rwell ) = ( 3.94e-09 ) ; ( R ) = ( 4.66e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.54e-03 ) ; ( Rwell ) = ( 2.32e-07 ) ; ( R ) = ( 6.54e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.98e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.10e-05 ) ; ( Rwell ) = ( 4.64e-08 ) ; ( R ) = ( 5.10e-05 ) ; + Last LinSolve(iter,res) = ( 4, 5.79e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26315301.54173911 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26526799.727356557 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 25997926.088479128 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.158692 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0769853 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.91779e+07s, dt:112712s, Cycle: 318 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.61e-02 ) ; ( Rwell ) = ( 4.70e-08 ) ; ( R ) = ( 4.61e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.02e-03 ) ; ( Rwell ) = ( 2.52e-07 ) ; ( R ) = ( 7.02e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.77e-05 ) ; ( Rwell ) = ( 6.44e-09 ) ; ( R ) = ( 5.77e-05 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26359006.5369528 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26569827.85799728 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 26041659.18040768 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.151818 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0671976 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.92906e+07s, dt:115802s, Cycle: 319 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.56e-02 ) ; ( Rwell ) = ( 6.89e-09 ) ; ( R ) = ( 4.56e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.86e-03 ) ; ( Rwell ) = ( 3.90e-07 ) ; ( R ) = ( 4.86e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.30e-05 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 2.30e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.35e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26404280.316187005 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26614389.968132693 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 26086956.923694342 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.151595 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0557441 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.94064e+07s, dt:133995s, Cycle: 320 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.39e-02 ) ; ( Rwell ) = ( 4.97e-09 ) ; ( R ) = ( 4.39e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.21e-02 ) ; ( Rwell ) = ( 2.03e-07 ) ; ( R ) = ( 2.21e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.09e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.35e-05 ) ; ( Rwell ) = ( 7.96e-08 ) ; ( R ) = ( 2.35e-05 ) ; + Last LinSolve(iter,res) = ( 4, 6.44e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26456519.446545467 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +wellControls2: BHP (at the specified reference elevation): 26665838.293854617 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26139208.9733233 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026387 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.173363 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0491219 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.95404e+07s, dt:167251s, Cycle: 321 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 8.02e-08 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.01e-02 ) ; ( Rwell ) = ( 6.56e-07 ) ; ( R ) = ( 2.01e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.04e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 8.57e-04 ) ; ( Rwell ) = ( 2.31e-08 ) ; ( R ) = ( 8.57e-04 ) ; + Last LinSolve(iter,res) = ( 4, 8.30e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26521380.55629127 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 26729665.331853285 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270263096 sm3/s +wellControls3: BHP (at the specified reference elevation): 26204053.658043247 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.214615 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0774019 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 2.97077e+07s, dt:156237s, Cycle: 322 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.24e-02 ) ; ( Rwell ) = ( 2.23e-08 ) ; ( R ) = ( 4.24e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.28e-02 ) ; ( Rwell ) = ( 5.13e-07 ) ; ( R ) = ( 1.28e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.11e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.33e-03 ) ; ( Rwell ) = ( 7.12e-08 ) ; ( R ) = ( 2.33e-03 ) ; + Last LinSolve(iter,res) = ( 4, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 8.03e-06 ) ; ( Rwell ) = ( 9.56e-09 ) ; ( R ) = ( 8.03e-06 ) ; + Last LinSolve(iter,res) = ( 3, 5.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26581764.028370716 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26789160.872423284 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 26264430.536942843 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.199103 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.057598 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 2.98639e+07s, dt:177162s, Cycle: 323 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.60e-02 ) ; ( Rwell ) = ( 1.02e-08 ) ; ( R ) = ( 4.60e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.10e-02 ) ; ( Rwell ) = ( 3.66e-07 ) ; ( R ) = ( 2.10e-02 ) ; + Last LinSolve(iter,res) = ( 5, 8.75e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.48e-03 ) ; ( Rwell ) = ( 1.16e-08 ) ; ( R ) = ( 1.48e-03 ) ; + Last LinSolve(iter,res) = ( 5, 8.84e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.58e-06 ) ; ( Rwell ) = ( 5.68e-11 ) ; ( R ) = ( 1.58e-06 ) ; + Last LinSolve(iter,res) = ( 6, 1.94e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26650705.435604762 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26857028.630370274 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 26333360.160502605 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.228081 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.111066 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.00411e+07s, dt:127354s, Cycle: 324 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.75e-02 ) ; ( Rwell ) = ( 9.71e-10 ) ; ( R ) = ( 4.75e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.71e-02 ) ; ( Rwell ) = ( 3.15e-07 ) ; ( R ) = ( 1.71e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.00e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.94e-04 ) ; ( Rwell ) = ( 4.44e-09 ) ; ( R ) = ( 5.94e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.82e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26700380.961331602 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 26906080.93644759 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26383035.94574738 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.164188 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0684034 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.01684e+07s, dt:129320s, Cycle: 325 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.25e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 4.25e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.62e-02 ) ; ( Rwell ) = ( 1.65e-07 ) ; ( R ) = ( 2.62e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.48e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.82e-03 ) ; ( Rwell ) = ( 7.84e-09 ) ; ( R ) = ( 1.82e-03 ) ; + Last LinSolve(iter,res) = ( 5, 9.44e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 1.69e-06 ) ; ( Rwell ) = ( 1.74e-10 ) ; ( R ) = ( 1.69e-06 ) ; + Last LinSolve(iter,res) = ( 5, 1.89e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26751032.161167156 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 26956036.217549007 Pa +wellControls2: Total rate: 56.32837354192297 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026515 sm3/s +wellControls3: BHP (at the specified reference elevation): 26433698.058140904 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537293 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.166981 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0524013 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.02977e+07s, dt:155359s, Cycle: 326 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 5.03e-02 ) ; ( Rwell ) = ( 9.70e-10 ) ; ( R ) = ( 5.03e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.18e-02 ) ; ( Rwell ) = ( 4.52e-07 ) ; ( R ) = ( 3.18e-02 ) ; + Last LinSolve(iter,res) = ( 5, 7.18e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.86e-04 ) ; ( Rwell ) = ( 2.25e-08 ) ; ( R ) = ( 9.86e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26811832.901997883 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27015968.911869098 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls3: BHP (at the specified reference elevation): 26494541.941107728 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.199526 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.101408 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.04531e+07s, dt:119588s, Cycle: 327 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.72e-02 ) ; ( Rwell ) = ( 2.31e-08 ) ; ( R ) = ( 4.72e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 4.79e-03 ) ; ( Rwell ) = ( 3.41e-07 ) ; ( R ) = ( 4.79e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.15e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.31e-05 ) ; ( Rwell ) = ( 6.91e-09 ) ; ( R ) = ( 3.31e-05 ) ; + Last LinSolve(iter,res) = ( 5, 3.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26858575.910603616 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27062045.68369454 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls3: BHP (at the specified reference elevation): 26541313.58754016 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.154389 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0743892 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.05727e+07s, dt:114790s, Cycle: 328 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 6.91e-09 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.93e-03 ) ; ( Rwell ) = ( 4.38e-07 ) ; ( R ) = ( 5.93e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.06e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 5.72e-05 ) ; ( Rwell ) = ( 2.35e-08 ) ; ( R ) = ( 5.72e-05 ) ; + Last LinSolve(iter,res) = ( 4, 4.37e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26903257.791840333 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27106083.556338467 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 26586000.239712738 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.148834 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0621201 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.06875e+07s, dt:124103s, Cycle: 329 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.32e-02 ) ; ( Rwell ) = ( 2.41e-08 ) ; ( R ) = ( 4.32e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.55e-02 ) ; ( Rwell ) = ( 1.39e-07 ) ; ( R ) = ( 1.55e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.95e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.02e-04 ) ; ( Rwell ) = ( 3.16e-09 ) ; ( R ) = ( 1.02e-04 ) ; + Last LinSolve(iter,res) = ( 5, 5.32e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26951504.856022608 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27153636.776272167 Pa +wellControls2: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls3: BHP (at the specified reference elevation): 26634258.19681451 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.16237 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0785337 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.08116e+07s, dt:114775s, Cycle: 330 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.41e-09 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.94e-02 ) ; ( Rwell ) = ( 4.70e-07 ) ; ( R ) = ( 1.94e-02 ) ; + Last LinSolve(iter,res) = ( 5, 5.29e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.76e-04 ) ; ( Rwell ) = ( 4.37e-08 ) ; ( R ) = ( 1.76e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.21e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 26995944.954055544 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026413 sm3/s +wellControls2: BHP (at the specified reference elevation): 27197461.28466131 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26678711.317049228 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.150617 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0811316 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.09264e+07s, dt:103773s, Cycle: 331 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.51e-02 ) ; ( Rwell ) = ( 4.43e-08 ) ; ( R ) = ( 4.51e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 5.89e-03 ) ; ( Rwell ) = ( 3.46e-07 ) ; ( R ) = ( 5.89e-03 ) ; + Last LinSolve(iter,res) = ( 5, 3.89e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 1.64e-05 ) ; ( Rwell ) = ( 7.43e-08 ) ; ( R ) = ( 1.64e-05 ) ; + Last LinSolve(iter,res) = ( 4, 7.75e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27036105.00922547 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls2: BHP (at the specified reference elevation): 27237074.13515038 Pa +wellControls2: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270265145 sm3/s +wellControls3: BHP (at the specified reference elevation): 26718890.800886977 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.136259 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0711568 +coupledFlowAndWells: Time-step required will be decreased based on state change. +Time: 3.10301e+07s, dt:102643s, Cycle: 332 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.46e-02 ) ; ( Rwell ) = ( 7.49e-08 ) ; ( R ) = ( 4.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.46e-02 ) ; ( Rwell ) = ( 3.75e-07 ) ; ( R ) = ( 1.46e-02 ) ; + Last LinSolve(iter,res) = ( 5, 4.72e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.14e-04 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 2.14e-04 ) ; + Last LinSolve(iter,res) = ( 6, 4.34e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27075891.161322135 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls2: BHP (at the specified reference elevation): 27276263.14470493 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 26758680.831821807 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.132538 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0638391 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.11328e+07s, dt:109041s, Cycle: 333 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.40e-02 ) ; ( Rwell ) = ( 4.88e-09 ) ; ( R ) = ( 4.40e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 7.18e-03 ) ; ( Rwell ) = ( 3.11e-07 ) ; ( R ) = ( 7.18e-03 ) ; + Last LinSolve(iter,res) = ( 5, 4.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.66e-05 ) ; ( Rwell ) = ( 3.00e-09 ) ; ( R ) = ( 4.66e-05 ) ; + Last LinSolve(iter,res) = ( 5, 7.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27118094.6393445 Pa +wellControls1: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026463 sm3/s +wellControls2: BHP (at the specified reference elevation): 27317872.46024215 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26800911.49818272 Pa +wellControls3: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270263866 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.139099 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0551158 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.12418e+07s, dt:127051s, Cycle: 334 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.31e-02 ) ; ( Rwell ) = ( 3.66e-09 ) ; ( R ) = ( 4.31e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.63e-03 ) ; ( Rwell ) = ( 1.33e-07 ) ; ( R ) = ( 9.63e-03 ) ; + Last LinSolve(iter,res) = ( 5, 5.93e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 6.50e-05 ) ; ( Rwell ) = ( 4.30e-09 ) ; ( R ) = ( 6.50e-05 ) ; + Last LinSolve(iter,res) = ( 5, 6.96e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27167113.806474622 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 27366228.516251996 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +wellControls3: BHP (at the specified reference elevation): 26849947.147123694 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.160511 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0605758 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.13689e+07s, dt:139578s, Cycle: 335 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 4.04e-02 ) ; ( Rwell ) = ( 4.71e-09 ) ; ( R ) = ( 4.04e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 3.13e-02 ) ; ( Rwell ) = ( 1.89e-07 ) ; ( R ) = ( 3.13e-02 ) ; + Last LinSolve(iter,res) = ( 5, 6.07e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 3.66e-04 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 3.66e-04 ) ; + Last LinSolve(iter,res) = ( 3, 5.12e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27220920.982754134 Pa +wellControls1: Total rate: 56.32837354192295 kg/s; total surface volumetric rate: 29.999999999999996 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.999722681537296 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.0002773184627026412 sm3/s +wellControls2: BHP (at the specified reference elevation): 27419302.069424786 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26903764.189188045 Pa +wellControls3: Total rate: 56.328373541922964 kg/s; total surface volumetric rate: 30.000000000000004 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.999722681537303 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264896 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.176579 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0560994 +coupledFlowAndWells: Time-step required will be increased based on state change. +Time: 3.15084e+07s, dt:27553.4s, Cycle: 336 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.92e-03 ) ; ( Rwell ) = ( 2.12e-08 ) ; ( R ) = ( 6.92e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 1.78e-04 ) ; ( Rwell ) = ( 3.26e-07 ) ; ( R ) = ( 1.78e-04 ) ; + Last LinSolve(iter,res) = ( 4, 4.11e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27231485.990047652 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27429799.143916663 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26914426.30185358 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0366509 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0106359 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.1536e+07s, dt:55106.9s, Cycle: 337 +compflowStatistics, Reservoir: Pressure (min, average, max): 2.80948e+07, 2.99421e+07, 3.12538e+07 Pa +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.3012e+07, 6.51497e+10 } kg +compflowStatistics, Caprock: Pressure (min, average, max): 2.76478e+07, 2.89944e+07, 2.98486e+07 Pa +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 2.19936e+07, 1.27238e+10 } kg +compflowStatistics: Max phase CFL number: 0.721008 +compflowStatistics: Max component CFL number: 1.15538 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 6.85e-07 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27252686.916117527 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27450836.07294756 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26935804.208137162 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0702061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0218585 +coupledFlowAndWells: Time-step required will be increased based on state change. \ No newline at end of file diff --git a/geos-posp/tests/Data/small_job_GEOS_825200_wells.out b/geos-posp/tests/Data/small_job_GEOS_825200_wells.out new file mode 100644 index 00000000..5a18738d --- /dev/null +++ b/geos-posp/tests/Data/small_job_GEOS_825200_wells.out @@ -0,0 +1,289 @@ +Num ranks: 1 +MKL max threads: 1 +GEOSX version: 0.2.0 (feature/dkachuma/allow-negative-pressure-with-errors, sha1: d15a5d5) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Started at 2023-06-20 16:04:54 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, SyntheticMesh +Adding Mesh: InternalWell, well_1 +Adding Mesh: InternalWell, well_2 +Adding Mesh: InternalWell, well_3 +Adding Event: PeriodicEvent, outputInjectionPeriod +Adding Event: PeriodicEvent, outputPostInjectionPeriod +Adding Event: PeriodicEvent, statistics +Adding Event: PeriodicEvent, solverApplicationsInjectionPeriod +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod1 +Adding Event: PeriodicEvent, solverApplicationsPostInjectionPeriod2 +Adding Output: VTK, vtkOutput + TableFunction: totalRateTable +Adding Object CellElementRegion named Reservoir from ObjectManager::Catalog. +Adding Object CellElementRegion named Caprock from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion1 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion2 from ObjectManager::Catalog. +Adding Object WellElementRegion named wellRegion3 from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: wellControls1_ConstantBHP_table + TableFunction: wellControls1_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table + TableFunction: wellControls2_ConstantBHP_table + TableFunction: wellControls2_ConstantPhaseRate_table + TableFunction: wellControls3_ConstantBHP_table + TableFunction: wellControls3_ConstantPhaseRate_table +VTKMesh 'SyntheticMesh': reading mesh from /scratchrd/GIS/OT/l1094441/TestJeanne/TestJeanne9C/ModelA.vtu +Generating global Ids from VTK mesh +VTKMesh 'SyntheticMesh': generating GEOSX mesh data structure +Importing cell block 0_tetrahedra +Importing cell block 3_tetrahedra +Importing cell block 1_tetrahedra +Importing cell block 4_tetrahedra +Importing cell block 2_tetrahedra +Number of nodes: 9188 + Number of elems: 48935 + C3D4: 48935 +Load balancing: min avg max +(element/rank): 48935 48935 48935 + +++++++++++++++++++++++++++ +InternalWellGenerator = well_1 +MPI rank = 0 + +Number of well elements = 3 +Well element #0 +Coordinates of the element center: { 400, 1400, 237.313 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 400, 1400, -79.354 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 400, 1400, -396.021 } +Next well element # = 1 +No previous well element +First well node: #2 +Second well node: #3 + +Number of perforations = 3 +Perforation #0 +Coordinates of the perforation: { 400, 1400, -15 } +Is connected to well element #1 +Perforation #1 +Coordinates of the perforation: { 400, 1400, -120.436 } +Is connected to well element #1 +Perforation #2 +Coordinates of the perforation: { 400, 1400, -350 } +Is connected to well element #2 + + +++++++++++++++++++++++++++ +InternalWellGenerator = well_2 +MPI rank = 0 + +Number of well elements = 2 +Well element #0 +Coordinates of the element center: { 1200, 742.759, 158.146 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 1200, 742.759, -316.854 } +Next well element # = 0 +No previous well element +First well node: #1 +Second well node: #2 + +Number of perforations = 2 +Perforation #0 +Coordinates of the perforation: { 1200, 742.759, 100 } +Is connected to well element #0 +Perforation #1 +Coordinates of the perforation: { 1200, 742.759, -500 } +Is connected to well element #1 + + +++++++++++++++++++++++++++ +InternalWellGenerator = well_3 +MPI rank = 0 + +Number of well elements = 5 +Well element #0 +Coordinates of the element center: { 800, 1450, 300.646 } +No next well element +Previous well element #1 +First well node: #0 +Second well node: #1 +Well element #1 +Coordinates of the element center: { 800, 1450, 110.646 } +Next well element # = 0 +Previous well element #2 +First well node: #1 +Second well node: #2 +Well element #2 +Coordinates of the element center: { 800, 1450, -79.354 } +Next well element # = 1 +Previous well element #3 +First well node: #2 +Second well node: #3 +Well element #3 +Coordinates of the element center: { 800, 1450, -269.354 } +Next well element # = 2 +Previous well element #4 +First well node: #3 +Second well node: #4 +Well element #4 +Coordinates of the element center: { 800, 1450, -459.354 } +Next well element # = 3 +No previous well element +First well node: #4 +Second well node: #5 + +Number of perforations = 5 +Perforation #0 +Coordinates of the perforation: { 800, 1450, 150 } +Is connected to well element #1 +Perforation #1 +Coordinates of the perforation: { 800, 1450, -30 } +Is connected to well element #2 +Perforation #2 +Coordinates of the perforation: { 800, 1450, -150 } +Is connected to well element #2 +Perforation #3 +Coordinates of the perforation: { 800, 1450, -325 } +Is connected to well element #3 +Perforation #4 +Coordinates of the perforation: { 800, 1450, -480 } +Is connected to well element #4 + +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Caprock, 4_tetrahedra +SyntheticMesh/Level0/Caprock/4_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Caprock/4_tetrahedra/rock_caprock allocated 1 quadrature points +SyntheticMesh/Level0/Caprock/4_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Overburden, 3_tetrahedra +SyntheticMesh/Level0/Overburden/3_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Overburden/3_tetrahedra/rock_burden allocated 1 quadrature points +SyntheticMesh/Level0/Overburden/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Reservoir, 2_tetrahedra +SyntheticMesh/Level0/Reservoir/2_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/2_tetrahedra/rock_reservoir allocated 1 quadrature points +SyntheticMesh/Level0/Reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Salt, 0_tetrahedra +SyntheticMesh/Level0/Salt/0_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Salt/0_tetrahedra/rock_salt allocated 1 quadrature points +SyntheticMesh/Level0/Salt/0_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, Underburden, 1_tetrahedra +SyntheticMesh/Level0/Underburden/1_tetrahedra/fluid allocated 1 quadrature points +SyntheticMesh/Level0/Underburden/1_tetrahedra/rock_burden allocated 1 quadrature points +SyntheticMesh/Level0/Underburden/1_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion1, wellRegion1UniqueSubRegion +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion1/wellRegion1UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion2, wellRegion2UniqueSubRegion +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion2/wellRegion2UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = SyntheticMesh, Level0, wellRegion3, wellRegion3UniqueSubRegion +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/fluid allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/relperm allocated 1 quadrature points +SyntheticMesh/Level0/wellRegion3/wellRegion3UniqueSubRegion/rockPerm_burden allocated 1 quadrature points +SyntheticMesh: importing field data from mesh dataset +Time: 0s, dt:100s, Cycle: 0 +compflowStatistics, Reservoir: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 0, 6.38235e+10 } kg +compflowStatistics, Caprock: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 0, 1.25037e+10 } kg +compflowStatistics: Max phase CFL number: 0.00696878 +compflowStatistics: Max component CFL number: 0.00696878 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.54e+02 ) ; ( R ) = ( 1.54e+02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 7.41e-01 ) ; ( R ) = ( 7.41e-01 ) ; + Last LinSolve(iter,res) = ( 1, 9.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.70e-05 ) ; ( Rwell ) = ( 9.97e-04 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 2, 4.23e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 12337146.157562563 Pa +wellControls1: Total rate: 56.37348443784919 kg/s; total surface volumetric rate: 30.024025669350802 sm3/s +wellControls1: Phase 0 surface volumetric rate: 30.023748128796043 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027754055475897704 sm3/s +wellControls2: BHP (at the specified reference elevation): 13268440.020500632 Pa +wellControls2: Total rate: 56.38455514210006 kg/s; total surface volumetric rate: 30.029921829787227 sm3/s +wellControls2: Phase 0 surface volumetric rate: 30.029644234728664 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.0002775950585639181 sm3/s +wellControls3: BHP (at the specified reference elevation): 12318458.650753867 Pa +wellControls3: Total rate: 56.379144772078966 kg/s; total surface volumetric rate: 30.027040313946728 sm3/s +wellControls3: Phase 0 surface volumetric rate: 30.02676274552475 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.0002775684219790799 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 2.40959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 5.78676e-09 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 1e6s, dt:1e6s, Cycle: 0 +compflowStatistics, Reservoir: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 0, 6.38235e+10 } kg +compflowStatistics, Caprock: Pressure (min, average, max): 1.25e+07, 1.25e+07, 1.25e+07 Pa +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 0, 1.25037e+10 } kg +compflowStatistics: Max phase CFL number: 0.00696878 +compflowStatistics: Max component CFL number: 0.00696878 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.01e-02 ) ; ( Rwell ) = ( 1.54e+02 ) ; ( R ) = ( 1.54e+02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 6.33e-04 ) ; ( Rwell ) = ( 7.41e-01 ) ; ( R ) = ( 7.41e-01 ) ; + Last LinSolve(iter,res) = ( 1, 9.38e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 4.70e-05 ) ; ( Rwell ) = ( 9.97e-04 ) ; ( R ) = ( 9.99e-04 ) ; + Last LinSolve(iter,res) = ( 2, 4.23e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 2.40959 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 5.78676e-09 +coupledFlowAndWells: Newton solver converged in less than 8 iterations, time-step required will be increased. +Time: 3.1536e+07s, dt:55106.9s, Cycle: 337 +compflowStatistics, Reservoir: Pressure (min, average, max): 2.80948e+07, 2.99421e+07, 3.12538e+07 Pa +compflowStatistics, Reservoir: Mobile phase mass (metric 2): { 1.3012e+07, 6.51497e+10 } kg +compflowStatistics, Caprock: Pressure (min, average, max): 2.76478e+07, 2.89944e+07, 2.98486e+07 Pa +compflowStatistics, Caprock: Mobile phase mass (metric 2): { 2.19936e+07, 1.27238e+10 } kg +compflowStatistics: Max phase CFL number: 0.721008 +compflowStatistics: Max component CFL number: 1.15538 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.33e-02 ) ; ( Rwell ) = ( 3.27e-07 ) ; ( R ) = ( 1.33e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 9.74e-04 ) ; ( Rwell ) = ( 6.85e-07 ) ; ( R ) = ( 9.74e-04 ) ; + Last LinSolve(iter,res) = ( 4, 7.03e-03 ) ; +wellControls1: BHP (at the specified reference elevation): 27252686.916117527 Pa +wellControls1: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls1: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls1: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +wellControls2: BHP (at the specified reference elevation): 27450836.07294756 Pa +wellControls2: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls2: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls2: Phase 1 surface volumetric rate: 0.00027731846270264126 sm3/s +wellControls3: BHP (at the specified reference elevation): 26935804.208137162 Pa +wellControls3: Total rate: 56.32837354192296 kg/s; total surface volumetric rate: 30 sm3/s +wellControls3: Phase 0 surface volumetric rate: 29.9997226815373 sm3/s +wellControls3: Phase 1 surface volumetric rate: 0.00027731846270264625 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0702061 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0218585 +coupledFlowAndWells: Time-step required will be increased based on state change. \ No newline at end of file diff --git a/geos-posp/tests/Data/small_job_GEOS_891567.out b/geos-posp/tests/Data/small_job_GEOS_891567.out new file mode 100644 index 00000000..4e79e48d --- /dev/null +++ b/geos-posp/tests/Data/small_job_GEOS_891567.out @@ -0,0 +1,175 @@ +GEOSX version: 0.2.0 (HEAD, sha1: 2e19665) + - c++ compiler: gcc 8.3.0 + - MPI version: Open MPI v2.1.5, package: Open MPI root@pandev07 Distribution, ident: 2.1.5, repo rev: v2.1.4-8-g697c1e9, Aug 15, 2018 + - HDF5 version: 1.12.1 + - Conduit version: 0.8.2 + - VTK version: 9.1.0 + - RAJA version: 2022.3.0 + - umpire version: 2022.3.0 + - adiak version: .. + - caliper version: 2.8.0 + - METIS version: 5.1.0 + - PARAMETIS version: 4.0.3 + - scotch version: 6.0.9 + - superlu_dist version: 6.3.0 + - suitesparse version: 5.7.9 + - hypre release version: 2.27.0 +Adding Solver of type CompositionalMultiphaseReservoir, named coupledFlowAndWells +Adding Solver of type CompositionalMultiphaseFVM, named compositionalMultiphaseFlow +Adding Solver of type CompositionalMultiphaseWell, named compositionalMultiphaseWell +Adding Mesh: VTKMesh, mesh +Adding Mesh: InternalWell, well_1 +Adding Event: PeriodicEvent, time_steps_1_output +Adding Event: PeriodicEvent, time_steps_1_applications +Adding Event: PeriodicEvent, time_steps_2_output +Adding Event: PeriodicEvent, time_steps_2_applications +Adding Event: PeriodicEvent, statistics +Adding Output: VTK, hexdom_well_module_multiphaseWell + TableFunction: totalRateTable +Adding Object CellElementRegion named caprock from ObjectManager::Catalog. +Adding Object CellElementRegion named reservoir from ObjectManager::Catalog. +Adding Object WellElementRegion named well_1region from ObjectManager::Catalog. + TableFunction: fluid_phaseModel1_PhillipsBrineDensity_table + TableFunction: fluid_phaseModel1_PhillipsBrineViscosity_table + TableFunction: fluid_phaseModel2_SpanWagnerCO2Density_table + TableFunction: fluid_phaseModel2_FenghourCO2Viscosity_table + TableFunction: fluid_CO2Solubility_table + TableFunction: well_1Control_ConstantBHP_table + TableFunction: well_1Control_ConstantPhaseRate_table + TableFunction: WellControls_OpenStatus_table +VTKMesh 'mesh': reading mesh from /work206/workrd/users/l1045328/job_GEOS/maillage_tresfin/TPFA/Wtrue/hexdom_Wtrue.vtu + reading the dataset... + redistributing mesh... +Generating global Ids from VTK mesh + finding neighbor ranks... + done! +VTKMesh 'mesh': generating GEOSX mesh data structure + preprocessing... + writing nodes... + writing cells... +Importing cell block 3_tetrahedra +Importing cell block 1_tetrahedra +Importing cell block 2_tetrahedra +Importing cell block 3_pyramids +Importing cell block 1_pyramids +Importing cell block 2_pyramids +Importing cell block 2_hexahedra +Importing cell block 3_hexahedra +Importing cell block 1_hexahedra + writing surfaces... +Importing surface 2 +Importing surface 3 +Importing surface 1 + building connectivity maps... + done! +Number of nodes: 2558433 + Number of elems: 3021450 + Polygon: 210306 + C3D4: 304106 + C3D5: 67546 + C3D8: 2439492 +Load balancing: min avg max +(element/rank): 4072 5901 6196 +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_hexahedra +mesh/Level0/caprock/1_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_hexahedra/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_pyramids +mesh/Level0/caprock/1_pyramids/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_pyramids/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, caprock, 1_tetrahedra +mesh/Level0/caprock/1_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/caprock/1_tetrahedra/rockregion_1 allocated 1 quadrature points +mesh/Level0/caprock/1_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_hexahedra +mesh/Level0/reservoir/2_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_pyramids +mesh/Level0/reservoir/2_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 2_tetrahedra +mesh/Level0/reservoir/2_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/2_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_hexahedra +mesh/Level0/reservoir/3_hexahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_hexahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_pyramids +mesh/Level0/reservoir/3_pyramids/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_pyramids/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, reservoir, 3_tetrahedra +mesh/Level0/reservoir/3_tetrahedra/fluid allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/rockregion allocated 1 quadrature points +mesh/Level0/reservoir/3_tetrahedra/relperm allocated 1 quadrature points +regionQuadrature: meshBodyName, meshLevelName, regionName, subRegionName = mesh, Level0, well_1region, well_1regionUniqueSubRegion +mesh/Level0/well_1region/well_1regionUniqueSubRegion/fluid allocated 1 quadrature points +mesh/Level0/well_1region/well_1regionUniqueSubRegion/relperm allocated 1 quadrature points +mesh/Level0/well_1region/well_1regionUniqueSubRegion/rockPermregion0 allocated 1 quadrature points +mesh: importing field data from mesh dataset +Time: 0s, dt:100s, Cycle: 0 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 1.09e-01 ) ; ( Rwell ) = ( 1.98e+01 ) ; ( R ) = ( 1.98e+01 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 2.57e-01 ) ; ( Rwell ) = ( 1.04e-01 ) ; ( R ) = ( 2.78e-01 ) ; + Last LinSolve(iter,res) = ( 1, 4.85e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 9.81e-02 ) ; ( Rwell ) = ( 1.84e-02 ) ; ( R ) = ( 9.98e-02 ) ; + Last LinSolve(iter,res) = ( 2, 4.69e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 3 + ( Rflow ) = ( 7.50e-03 ) ; ( Rwell ) = ( 3.96e-04 ) ; ( R ) = ( 7.51e-03 ) ; + Last LinSolve(iter,res) = ( 2, 4.40e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 4 + ( Rflow ) = ( 1.65e-04 ) ; ( Rwell ) = ( 4.54e-05 ) ; ( R ) = ( 1.71e-04 ) ; + Last LinSolve(iter,res) = ( 3, 3.34e-03 ) ; +compositionalMultiphaseFlow: Max relative pressure change: 4.89251 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.171291 +coupledFlowAndWells: Time-step required will be decreased based on state change. +compflowStatistics, reservoir: Pressure (min, average, max): 1.24938e+07, 1.25001e+07, 1.31116e+07 Pa +compflowStatistics, reservoir: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, reservoir: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, reservoir: Total dynamic pore volume: 728.734 rm^3 +compflowStatistics, reservoir: Phase dynamic pore volumes: { 3.94665e-05, 728.734 } rm^3 +compflowStatistics, reservoir: Phase mass: { 0.0113525, 703284 } kg +compflowStatistics, reservoir: Trapped phase mass (metric 1): { 0.00331405, 210985 } kg +compflowStatistics, reservoir: Non-trapped phase mass (metric 1): { 0.00803841, 492299 } kg +compflowStatistics, reservoir: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, reservoir: Mobile phase mass (metric 2): { 0.0113525, 703284 } kg +compflowStatistics, reservoir: Dissolved component mass: { { 0.0113525, 0 }, { 0.0174064, 703284 } } kg +compflowStatistics, caprock: Pressure (min, average, max): 1.24954e+07, 1.25e+07, 1.25003e+07 Pa +compflowStatistics, caprock: Delta pressure (min, max): 0, 0 Pa +compflowStatistics, caprock: Temperature (min, average, max): 368.15, 368.15, 368.15 K +compflowStatistics, caprock: Total dynamic pore volume: 222.653 rm^3 +compflowStatistics, caprock: Phase dynamic pore volumes: { 0, 222.653 } rm^3 +compflowStatistics, caprock: Phase mass: { 0, 214877 } kg +compflowStatistics, caprock: Trapped phase mass (metric 1): { 0, 64463.1 } kg +compflowStatistics, caprock: Non-trapped phase mass (metric 1): { 0, 150414 } kg +compflowStatistics, caprock: Immobile phase mass (metric 2): { 0, 0 } kg +compflowStatistics, caprock: Mobile phase mass (metric 2): { 0, 214877 } kg +compflowStatistics, caprock: Dissolved component mass: { { 0, 0 }, { 2.22653e-08, 214877 } } kg +well_1Control: BHP (at the specified reference elevation): 23960094.51907003 Pa +well_1Control: Total rate: 0.00029566997749602594 kg/s; total surface volumetric rate: 2.0000000000000063e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.9999999999987377e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543855673e-17 sm3/s +compflowStatistics: Max phase CFL number: 1.57174 +compflowStatistics: Max component CFL number: 0.540281 +Time: 100s, dt:50.8989s, Cycle: 1 + Attempt: 0, ConfigurationIter: 0, NewtonIter: 0 + ( Rflow ) = ( 6.46e-02 ) ; ( Rwell ) = ( 1.19e-03 ) ; ( R ) = ( 6.46e-02 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 1 + ( Rflow ) = ( 8.01e-03 ) ; ( Rwell ) = ( 2.37e-03 ) ; ( R ) = ( 8.35e-03 ) ; + Last LinSolve(iter,res) = ( 2, 8.28e-03 ) ; + Attempt: 0, ConfigurationIter: 0, NewtonIter: 2 + ( Rflow ) = ( 2.42e-04 ) ; ( Rwell ) = ( 3.66e-05 ) ; ( R ) = ( 2.44e-04 ) ; + Last LinSolve(iter,res) = ( 2, 6.56e-03 ) ; +well_1Control: BHP (at the specified reference elevation): 23318529.329811733 Pa +well_1Control: Total rate: 0.00029566997749602507 kg/s; total surface volumetric rate: 2e-05 sm3/s +well_1Control: Phase 0 surface volumetric rate: 1.999999999998732e-05 sm3/s +well_1Control: Phase 1 surface volumetric rate: 1.2681312543888312e-17 sm3/s +compositionalMultiphaseFlow: Max relative pressure change: 0.0983323 % +compositionalMultiphaseFlow: Max absolute phase volume fraction change: 0.0741088 +coupledFlowAndWells: Time-step required will be decreased based on state change. \ No newline at end of file diff --git a/geos-posp/tests/__init__.py b/geos-posp/tests/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-posp/tests/mainTests.py b/geos-posp/tests/mainTests.py new file mode 100644 index 00000000..dec770fb --- /dev/null +++ b/geos-posp/tests/mainTests.py @@ -0,0 +1,26 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +import os +import sys +import unittest + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + + +def main() -> None: + """Run all tests.""" + # Load all test cases in the current folder + test_loader = unittest.TestLoader() + test_suite = test_loader.discover(".", pattern="tests*.py") + + # Run the test suite + runner = unittest.TextTestRunner() + runner.run(test_suite) + + +if __name__ == "__main__": + main() diff --git a/geos-posp/tests/testsCollectionSet.py b/geos-posp/tests/testsCollectionSet.py new file mode 100644 index 00000000..ef7f108d --- /dev/null +++ b/geos-posp/tests/testsCollectionSet.py @@ -0,0 +1,245 @@ +# SPDX-License-Identifier: Apache-2.0 +# # SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.processing.ConnectionSet import ( + ConnectionSet, + ConnectionSetCollection, +) + +faceId1: int = 1 +faceId2: int = 2 +faceId3: int = 10 +cellIdSide1: dict[int, bool] = {3: True, 4: False, 5: True} +cellIdSide2: dict[int, bool] = {6: True, 7: False, 4: True} +cellIdSide3: dict[int, bool] = {3: True, 6: False, 5: True} + + +class TestsConnectionSet(unittest.TestCase): + + def test_ConnectionSetInit(self: Self) -> None: + """Test ConnectionSet instanciation.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + self.assertEqual(cs1.getCellIdRef(), faceId1) + self.assertEqual(cs1.getConnectedCellIds(), cellIdSide1) + + def test_ConnectionSetEqual(self: Self) -> None: + """Test ConnectionSet equality.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide1) + cs3: ConnectionSet = ConnectionSet(faceId1, cellIdSide2) + + self.assertEqual(cs1, cs1) + self.assertNotEqual(cs1, cs2) + self.assertNotEqual(cs1, cs3) + + def test_ConnectionSetSetFaceId(self: Self) -> None: + """Test ConnectionSet SetFaceId method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs1.setCellIdRef(faceId2) + self.assertEqual(cs1.getCellIdRef(), faceId2) + + def test_ConnectionSetSetConnectedCellIds(self: Self) -> None: + """Test ConnectionSet SetConnectedCellIds method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs1.setConnectedCellIds(cellIdSide2) + self.assertEqual(cs1.getConnectedCellIds(), cellIdSide2) + + def test_ConnectionSetCopy(self: Self) -> None: + """Test ConnectionSet copy method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = cs1.copy() + self.assertFalse(cs1 is cs2) + self.assertEqual(cs1, cs2) + + def test_ConnectionSetAddConnectedCellIds(self: Self) -> None: + """Test ConnectionSet AddConnectedCellIds method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + expected: dict[int, bool] = {3: True, 4: True, 5: True, 6: True, 7: False} + cs1.addConnectedCells(cellIdSide2) + self.assertEqual(cs1.getConnectedCellIds(), expected) + + def test_ConnectionSetCollectionInit(self: Self) -> None: + """Test ConnectionSetCollection instanciation and add method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + self.assertEqual(len(csc), 2) + + def test_ConnectionSetCollectionAddMultiple(self: Self) -> None: + """Test ConnectionSetCollection addMultiple method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.addMultiple((cs1, cs2)) + + self.assertEqual(len(csc), 2) + + def test_ConnectionSetContains(self: Self) -> None: + """Test ConnectionSetCollection __contains__ method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + cs3: ConnectionSet = ConnectionSet(faceId3, cellIdSide1) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + self.assertTrue(cs1 in csc) + self.assertTrue(cs2 in csc) + self.assertTrue(cs3 not in csc) + + def test_ConnectionSetContainsCellIdRef(self: Self) -> None: + """Test ConnectionSetCollection containsCellIdRef method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + self.assertTrue(csc.containsCellIdRef(faceId1)) + self.assertTrue(csc.containsCellIdRef(faceId2)) + self.assertFalse(csc.containsCellIdRef(faceId3)) + + def test_ConnectionSetContainsEqual(self: Self) -> None: + """Test ConnectionSetCollection containsEqual method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + cs3: ConnectionSet = ConnectionSet(faceId1, cellIdSide3) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + self.assertTrue(csc.containsEqual(cs1)) + csc.replace(cs3) + + self.assertTrue(not csc.containsEqual(cs1)) + self.assertTrue(csc.containsEqual(cs3)) + + def test_ConnectionSetReplace(self: Self) -> None: + """Test ConnectionSetCollection replace method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + cs3: ConnectionSet = ConnectionSet(faceId1, cellIdSide3) + + print(cs1) + print(cs2) + print(cs3) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + print(csc) + csc.replace(cs3) + print(csc) + self.assertTrue(not csc.containsEqual(cs1)) + self.assertTrue(cs2 in csc) + self.assertTrue(cs3 in csc) + + def test_ConnectionSetGet(self: Self) -> None: + """Test ConnectionSetCollection get method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + self.assertEqual(csc.get(faceId1), cs1) + self.assertTrue(csc.get(faceId3) is None) + + def test_ConnectionSetDiscard(self: Self) -> None: + """Test ConnectionSetCollection discard method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + csc.discard(cs1) + + self.assertTrue(cs1 not in csc) + self.assertTrue(cs2 in csc) + + def test_ConnectionSetDiscardFaceId(self: Self) -> None: + """Test ConnectionSetCollection discardFaceId method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + csc.discardCellIdRef(faceId1) + + self.assertTrue(cs1 not in csc) + self.assertTrue(cs2 in csc) + + def test_ConnectionSetUpdate(self: Self) -> None: + """Test ConnectionSetCollection update method.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + cs3: ConnectionSet = ConnectionSet(faceId3, cellIdSide3) + cs4: ConnectionSet = ConnectionSet(faceId2, cellIdSide3) + + # expected cs2 + cs4 + cs5: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + cs5.addConnectedCells(cellIdSide3) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + + csc.update(cs3) + csc.update(cs4) + + self.assertTrue(cs1 in csc) + self.assertTrue(cs3 in csc) + self.assertTrue(cs5 in csc) + + def tests_GetReversedConnectionSetCollection(self: Self) -> None: + """Test ConnectionSetCollection getReversedConnectionSetCollection.""" + cs1: ConnectionSet = ConnectionSet(faceId1, cellIdSide1) + cs2: ConnectionSet = ConnectionSet(faceId2, cellIdSide2) + cs3: ConnectionSet = ConnectionSet(faceId3, cellIdSide3) + cs4: ConnectionSet = ConnectionSet(faceId2, cellIdSide3) + + csc: ConnectionSetCollection = ConnectionSetCollection() + csc.add(cs1) + csc.add(cs2) + csc.update(cs3) + csc.update(cs4) + + print(csc) + # expected results + cs21: ConnectionSet = ConnectionSet( + 3, {faceId1: True, faceId2: True, faceId3: True} + ) + cs22: ConnectionSet = ConnectionSet(4, {faceId1: False, faceId2: True}) + cs23: ConnectionSet = ConnectionSet(5, {faceId1: True, faceId3: True}) + cs24: ConnectionSet = ConnectionSet(6, {faceId2: True, faceId3: False}) + cs25: ConnectionSet = ConnectionSet(7, {faceId2: False}) + expected: ConnectionSetCollection = ConnectionSetCollection() + expected.addMultiple((cs21, cs22, cs23, cs24, cs25)) + + obtained: ConnectionSetCollection = csc.getReversedConnectionSetCollection() + self.assertEqual(obtained, expected) diff --git a/geos-posp/tests/testsFunctionsFigure2DGenerator.py b/geos-posp/tests/testsFunctionsFigure2DGenerator.py new file mode 100644 index 00000000..43f5ec0c --- /dev/null +++ b/geos-posp/tests/testsFunctionsFigure2DGenerator.py @@ -0,0 +1,183 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.visu.pythonViewUtils import functionsFigure2DGenerator as utils + + +class TestsFunctionsFigure2DGenerator(unittest.TestCase): + def test_associatePropertyToAxeType(self: Self) -> None: + """Test of associatePropertyToAxeType function.""" + example: list[str] = [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1", + "WellControls1__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1", + "WellControls2__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls3__BHP__Pa__Source1", + "WellControls3__TotalMassRate__tons/day__Source1", + "WellControls3__TotalSurfaceVolumetricRate__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateCO2__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateWater__bbl/day__Source1", + "Mean__BHP__Pa__Source1", + "Mean__TotalMassRate__tons/day__Source1", + "Mean_TotalVolumetricRate__bbl/day__Source1", + "Mean__SurfaceVolumetricRateCO2__bbl/day__Source1", + "Mean__SurfaceVolumetricRateWater__bbl/day__Source1", + ] + expected: dict[str, list[str]] = { + "BHP (Pa)": [ + "WellControls1__BHP__Pa__Source1", + "WellControls2__BHP__Pa__Source1", + "WellControls3__BHP__Pa__Source1", + "Mean__BHP__Pa__Source1", + ], + "MassRate (kg/s)": [ + "WellControls1__TotalMassRate__kg/s__Source1", + "WellControls2__TotalMassRate__kg/s__Source1", + ], + "VolumetricRate (m3/s)": [ + "WellControls1__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls2__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateWater__m3/s__Source1", + ], + "MassRate (tons/day)": [ + "WellControls3__TotalMassRate__tons/day__Source1", + "Mean__TotalMassRate__tons/day__Source1", + ], + "VolumetricRate (bbl/day)": [ + "WellControls3__TotalSurfaceVolumetricRate__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateCO2__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateWater__bbl/day__Source1", + "Mean_TotalVolumetricRate__bbl/day__Source1", + "Mean__SurfaceVolumetricRateCO2__bbl/day__Source1", + "Mean__SurfaceVolumetricRateWater__bbl/day__Source1", + ], + } + obtained: dict[str, list[str]] = utils.associatePropertyToAxeType(example) + self.assertEqual(expected, obtained) + + def test_propertiesPerIdentifier(self: Self) -> None: + """Test of propertiesPerIdentifier function.""" + propertyNames: list[str] = [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1", + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1", + ] + expected: dict[str, list[str]] = { + "WellControls1": [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1", + ], + "WellControls2": [ + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1", + ], + } + obtained = utils.propertiesPerIdentifier(propertyNames) + self.assertEqual(expected, obtained) + + def test_associationIdentifers(self: Self) -> None: + """Test of associationIdentifiers function.""" + propertyNames: list[str] = [ + "WellControls1__BHP__Pa__Source1", + "WellControls1__TotalMassRate__kg/s__Source1", + "WellControls1__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls2__BHP__Pa__Source1", + "WellControls2__TotalMassRate__kg/s__Source1", + "WellControls2__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateWater__m3/s__Source1", + "WellControls3__BHP__Pa__Source1", + "WellControls3__TotalMassRate__tons/day__Source1", + "WellControls3__TotalSurfaceVolumetricRate__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateCO2__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateWater__bbl/day__Source1", + "Mean__BHP__Pa__Source1", + "Mean__TotalMassRate__tons/day__Source1", + "Mean__TotalSurfaceVolumetricRate__bbl/day__Source1", + "Mean__SurfaceVolumetricRateCO2__bbl/day__Source1", + "Mean__SurfaceVolumetricRateWater__bbl/day__Source1", + ] + expected: dict[str, dict[str, list[str]]] = { + "WellControls1": { + "BHP (Pa)": [ + "WellControls1__BHP__Pa__Source1", + ], + "MassRate (kg/s)": [ + "WellControls1__TotalMassRate__kg/s__Source1", + ], + "VolumetricRate (m3/s)": [ + "WellControls1__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls1__SurfaceVolumetricRateWater__m3/s__Source1", + ], + }, + "WellControls2": { + "BHP (Pa)": [ + "WellControls2__BHP__Pa__Source1", + ], + "MassRate (kg/s)": [ + "WellControls2__TotalMassRate__kg/s__Source1", + ], + "VolumetricRate (m3/s)": [ + "WellControls2__TotalSurfaceVolumetricRate__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateCO2__m3/s__Source1", + "WellControls2__SurfaceVolumetricRateWater__m3/s__Source1", + ], + }, + "WellControls3": { + "BHP (Pa)": [ + "WellControls3__BHP__Pa__Source1", + ], + "MassRate (tons/day)": [ + "WellControls3__TotalMassRate__tons/day__Source1", + ], + "VolumetricRate (bbl/day)": [ + "WellControls3__TotalSurfaceVolumetricRate__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateCO2__bbl/day__Source1", + "WellControls3__SurfaceVolumetricRateWater__bbl/day__Source1", + ], + }, + "Mean": { + "BHP (Pa)": [ + "Mean__BHP__Pa__Source1", + ], + "MassRate (tons/day)": [ + "Mean__TotalMassRate__tons/day__Source1", + ], + "VolumetricRate (bbl/day)": [ + "Mean__TotalSurfaceVolumetricRate__bbl/day__Source1", + "Mean__SurfaceVolumetricRateCO2__bbl/day__Source1", + "Mean__SurfaceVolumetricRateWater__bbl/day__Source1", + ], + }, + } + obtained = utils.associationIdentifiers(propertyNames) + self.assertEqual(expected, obtained) + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsFunctionsGeomechanicsCalculator.py b/geos-posp/tests/testsFunctionsGeomechanicsCalculator.py new file mode 100644 index 00000000..9a8b2ead --- /dev/null +++ b/geos-posp/tests/testsFunctionsGeomechanicsCalculator.py @@ -0,0 +1,382 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +# SPDX-License-Identifier: Apache 2.0 +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +import numpy as np +import numpy.typing as npt +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import geos_posp.processing.geomechanicsCalculatorFunctions as fcts +from geos_posp.utils import PhysicalConstants +from geos_posp.utils.geosUtils import getAttributeMatrixFromVector +from geos_posp.utils.UnitRepository import Unit, UnitRepository + +# geomechanical outputs - Testing variables - Unit is GPa +bulkModulus: npt.NDArray[np.float64] = np.array([9.0, 50.0, 65.0, np.nan, 150.0]) +shearModulus: npt.NDArray[np.float64] = np.array([3.2, 24.0, np.nan, 70.0, 100.0]) +poissonRatio: npt.NDArray[np.float64] = np.array([0.34, 0.29, np.nan, np.nan, 0.23]) +density: npt.NDArray[np.float64] = np.array([2600.0, 3100.0, 2800.0, np.nan, 2900.0]) +biotCoefficient: npt.NDArray[np.float64] = np.array([0.1, 0.3, np.nan, 0.5, 0.6]) +pressure: npt.NDArray[np.float64] = np.array([10.0, 280.0, np.nan, 80.0, 100.0]) +effectiveStress: npt.NDArray[np.float64] = -1.0 * np.array( + [ + [160.0, 250.0, 180.0, np.nan, 200.0, 190.0], + [180.0, 260.0, 190.0, np.nan, 220.0, 210.0], + [200.0, 280.0, 210.0, np.nan, 230.0, 230.0], + [220.0, 290.0, 220.0, np.nan, 250.0, 250.0], + [260.0, 310.0, 230.0, np.nan, 290.0, 270.0], + ] +) +verticalStress: npt.NDArray[np.float64] = effectiveStress[:, 2] +horizontalStress: npt.NDArray[np.float64] = np.min(effectiveStress[:, :2], axis=1) + +stressVector: npt.NDArray[np.float64] = np.array([1.8, 2.5, 5.2, 0.3, 0.4, 0.1]) +stressTensor: npt.NDArray[np.float64] = getAttributeMatrixFromVector(stressVector) + + +class TestsFunctionsGeomechanicsCalculator(unittest.TestCase): + def test_SpecificGravity(self: Self) -> None: + """Test calculation of specific Gravity.""" + specificDensity: float = 1000.0 + + obtained: npt.NDArray[np.float64] = fcts.specificGravity( + density, specificDensity + ) + expected: npt.NDArray[np.float64] = np.array([2.6, 3.1, 2.8, np.nan, 2.9]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_YoungModulus(self: Self) -> None: + """Test calculation of young Modulus.""" + obtained: npt.NDArray[np.float64] = fcts.youngModulus(bulkModulus, shearModulus) + expected: npt.NDArray[np.float64] = np.array( + [8.58, 62.07, np.nan, np.nan, 245.45] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_PoissonRatio(self: Self) -> None: + """Test calculation of poisson Ratio.""" + obtained: npt.NDArray[np.float64] = fcts.poissonRatio(bulkModulus, shearModulus) + expected: npt.NDArray[np.float64] = np.array([0.34, 0.29, np.nan, np.nan, 0.23]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_BulkModulus(self: Self) -> None: + """Test calculation of bulk Modulus.""" + E: npt.NDArray[np.float64] = fcts.youngModulus(bulkModulus, shearModulus) + u: npt.NDArray[np.float64] = fcts.poissonRatio(bulkModulus, shearModulus) + + obtained: npt.NDArray[np.float64] = fcts.bulkModulus(E, u) + expected: npt.NDArray[np.float64] = bulkModulus + expected[2] = np.nan + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_ShearModulus(self: Self) -> None: + """Test calculation of shear Modulus.""" + E: npt.NDArray[np.float64] = fcts.youngModulus(bulkModulus, shearModulus) + u: npt.NDArray[np.float64] = fcts.poissonRatio(bulkModulus, shearModulus) + + obtained: npt.NDArray[np.float64] = fcts.shearModulus(E, u) + expected: npt.NDArray[np.float64] = shearModulus + expected[3] = np.nan + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_lambdaCoefficient(self: Self) -> None: + """Test calculation of shear Modulus.""" + E: npt.NDArray[np.float64] = fcts.youngModulus(bulkModulus, shearModulus) + u: npt.NDArray[np.float64] = fcts.poissonRatio(bulkModulus, shearModulus) + + obtained: npt.NDArray[np.float64] = fcts.lambdaCoefficient(E, u) + expected: npt.NDArray[np.float64] = np.array( + [6.87, 34.0, np.nan, np.nan, 83.33] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_OedometricModulus(self: Self) -> None: + """Test calculation of oedometric Modulus.""" + Edef: npt.NDArray[np.float64] = np.array([9.0, 50.0, 65.0, np.nan, 150.0]) + + obtained: npt.NDArray[np.float64] = fcts.oedometricModulus(Edef, poissonRatio) + expected: npt.NDArray[np.float64] = np.array( + [13.85, 65.52, np.nan, np.nan, 173.89] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_BiotCoefficient(self: Self) -> None: + """Test calculation of biot Coefficient.""" + Kgrain: float = 150.0 + obtained: npt.NDArray[np.float64] = fcts.biotCoefficient(Kgrain, bulkModulus) + expected: npt.NDArray[np.float64] = np.array([0.94, 0.67, 0.57, np.nan, 0.0]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_TotalStress(self: Self) -> None: + """Test calculation of Total Stress.""" + obtained: npt.NDArray[np.float64] = fcts.totalStress( + effectiveStress, biotCoefficient, pressure + ) + expected: npt.NDArray[np.float64] = np.array( + [ + [-161.0, -251.0, -181.0, np.nan, -200.0, -190.0], + [-264.0, -344.0, -274.0, np.nan, -220.0, -210.0], + [np.nan, np.nan, np.nan, np.nan, -230.0, -230.0], + [-260.0, -330.0, -260.0, np.nan, -250.0, -250.0], + [-320.0, -370.0, -290.0, np.nan, -290.0, -270.0], + ] + ) + + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_StressRatio(self: Self) -> None: + """Test calculation of Stress Ratio.""" + obtained: npt.NDArray[np.float64] = fcts.stressRatio( + horizontalStress, verticalStress + ) + expected: npt.NDArray[np.float64] = np.array([1.39, 1.37, 1.33, 1.32, 1.35]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_LithostaticStress(self: Self) -> None: + """Test calculation of lithostatic Stress.""" + zCoords: npt.NDArray[np.float64] = np.array( + [-2.0, -100.0, -500.0, np.nan, -2500.0] + ) + gravity: float = PhysicalConstants.GRAVITY + + obtained: npt.NDArray[np.float64] = fcts.lithostaticStress( + zCoords, density, gravity + ) + expected: npt.NDArray[np.float64] = np.array( + [51012.0, 3041100.0, 13734000.0, np.nan, 71122500.0] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_ElasticStrainFromBulkShear(self: Self) -> None: + """Test calculation of Elastic Strain.""" + deltaEffectiveStress: npt.NDArray[np.float64] = -1.3 * effectiveStress + deltaEffectiveStress[np.isnan(deltaEffectiveStress)] = 150.0 + obtained: npt.NDArray[np.float64] = fcts.elasticStrainFromBulkShear( + deltaEffectiveStress, bulkModulus, shearModulus + ) + expected: npt.NDArray[np.float64] = np.array( + [ + [2.02, 20.3, 6.08, 46.88, 81.25, 77.19], + [1.01, 3.17, 1.28, 6.25, 11.92, 11.38], + [np.nan, np.nan, np.nan, np.nan, np.nan, np.nan], + [np.nan, np.nan, np.nan, np.nan, np.nan, np.nan], + [0.73, 1.05, 0.53, 1.5, 3.77, 3.51], + ] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_ElasticStrainFromYoungPoisson(self: Self) -> None: + """Test calculation of Elastic Strain.""" + deltaEffectiveStress: npt.NDArray[np.float64] = -1.3 * effectiveStress + deltaEffectiveStress[np.isnan(deltaEffectiveStress)] = 150.0 + young: npt.NDArray[np.float64] = fcts.youngModulus(bulkModulus, shearModulus) + obtained: npt.NDArray[np.float64] = fcts.elasticStrainFromYoungPoisson( + deltaEffectiveStress, young, poissonRatio + ) + print(np.round(obtained, 2).tolist()) + + expected: npt.NDArray[np.float64] = np.array( + [ + [2.09, 20.36, 6.15, 46.84, 81.19, 77.13], + [1.04, 3.2, 1.31, 6.24, 11.89, 11.35], + [np.nan, np.nan, np.nan, np.nan, np.nan, np.nan], + [np.nan, np.nan, np.nan, np.nan, np.nan, np.nan], + [0.72, 1.04, 0.52, 1.5, 3.78, 3.52], + ] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_DeviatoricStressPathOed(self: Self) -> None: + """Test calculation of deviatoric Stress Path Oedometric conditions.""" + obtained: npt.NDArray[np.float64] = fcts.deviatoricStressPathOed(poissonRatio) + expected: npt.NDArray[np.float64] = np.array([0.52, 0.41, np.nan, np.nan, 0.3]) + + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_ReservoirStressPathReal(self: Self) -> None: + """Test calculation of reservoir Stress Path Real conditions.""" + deltaStress: npt.NDArray[np.float64] = -0.1 * effectiveStress + deltaPressure: npt.NDArray[np.float64] = 0.2 * pressure + obtained: npt.NDArray[np.float64] = fcts.reservoirStressPathReal( + deltaStress, deltaPressure + ) + expected: npt.NDArray[np.float64] = np.array( + [ + [8.0, 12.5, 9.0], + [0.32, 0.46, 0.34], + [np.nan, np.nan, np.nan], + [1.38, 1.81, 1.38], + [1.30, 1.55, 1.15], + ] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_ReservoirStressPathOed(self: Self) -> None: + """Test calculation of reservoir Stress Path Oedometric conditions.""" + obtained: npt.NDArray[np.float64] = fcts.reservoirStressPathOed( + biotCoefficient, poissonRatio + ) + expected: npt.NDArray[np.float64] = np.array([0.05, 0.18, np.nan, np.nan, 0.42]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_criticalTotalStressRatio(self: Self) -> None: + """Test calculation of fracture Index.""" + obtained: npt.NDArray[np.float64] = fcts.criticalTotalStressRatio( + pressure, verticalStress + ) + expected: npt.NDArray[np.float64] = np.array([0.06, 1.47, np.nan, 0.36, 0.43]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_totalStressRatioThreshold(self: Self) -> None: + """Test calculation of fracture Threshold.""" + obtained: npt.NDArray[np.float64] = fcts.totalStressRatioThreshold( + pressure, horizontalStress + ) + expected: npt.NDArray[np.float64] = np.array([0.04, 1.08, np.nan, 0.28, 0.32]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_CriticalPorePressure(self: Self) -> None: + """Test calculation of critical Pore Pressure.""" + rockCohesion: float = 20 # GPa + frictionAngle: float = 30 * np.pi / 180.0 # friction angle in radian + effectiveStress2: npt.NDArray[np.float64] = -1.0 * effectiveStress + effectiveStress2[np.isnan(effectiveStress)] = 180.0 + obtained: npt.NDArray[np.float64] = fcts.criticalPorePressure( + effectiveStress2, rockCohesion, frictionAngle + ) + expected: npt.NDArray[np.float64] = np.array( + [-302.43, -333.72, -348.1, -383.01, -438.03] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_CriticalPorePressureThreshold(self: Self) -> None: + """Test calculation of critical Pore Pressure Index.""" + criticalPorePressure: npt.NDArray[np.float64] = np.array( + [149.64, 174.64, 194.64, 219.64, 224.64] + ) + + obtained: npt.NDArray[np.float64] = fcts.criticalPorePressureThreshold( + pressure, criticalPorePressure + ) + expected: npt.NDArray[np.float64] = np.array([0.07, 1.6, np.nan, 0.36, 0.45]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_compressibility(self: Self) -> None: + """Test calculation of compressibility from elastic moduli.""" + porosity: npt.NDArray[np.float64] = np.array([0.05, 0.1, 0.15, 0.30, 0.20]) + + # multiply by 1000 to prevent from to small values + obtained: npt.NDArray[np.float64] = 1000.0 * fcts.compressibility( + poissonRatio, bulkModulus, biotCoefficient, porosity + ) + expected: npt.NDArray[np.float64] = np.array( + [110.438, 49.016, np.nan, np.nan, 18.991] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 3), np.round(expected, 3), equal_nan=True) + ) + + def test_shearCapacityUtilization(self: Self) -> None: + """Test calculation of shear capacity utilization.""" + # inputs + traction: npt.NDArray[np.float64] = np.copy(effectiveStress[:, :3]) + # replace nan values for calculation + traction[np.isnan(traction)] = 150.0 + rockCohesion = 250.0 + frictionAngle = 10.0 * np.pi / 180.0 + + # calculation + obtained: npt.NDArray[np.float64] = fcts.shearCapacityUtilization( + traction, rockCohesion, frictionAngle + ) + expected: npt.NDArray[np.float64] = np.array( + [0.899, 0.923, 0.982, 1.004, 1.048] + ) + + self.assertSequenceEqual( + np.round(obtained, 3).flatten().tolist(), expected.tolist() + ) + + def test_computeStressPrincipalComponents(self: Self) -> None: + """Test calculation of stress principal components from stress tensor.""" + obtained: list[float] = [ + round(val, 3) for val in fcts.computeStressPrincipalComponents(stressTensor) + ] + expected: tuple[float, float, float] = (1.748, 2.471, 5.281) + self.assertSequenceEqual(tuple(obtained), expected) + + def test_computeStressPrincipalComponentsFromStressVector(self: Self) -> None: + """Test calculation of stress principal components from stress vector.""" + obtained: list[float] = [ + round(val, 3) + for val in fcts.computeStressPrincipalComponentsFromStressVector( + stressVector + ) + ] + expected: tuple[float, float, float] = (1.748, 2.471, 5.281) + self.assertSequenceEqual(tuple(obtained), expected) + + def test_computeNormalShearStress(self: Self) -> None: + """Test calculation of normal and shear stress.""" + directionVector = np.array([1.0, 1.0, 0.0]) + obtained: list[float] = [ + round(val, 3) + for val in fcts.computeNormalShearStress(stressTensor, directionVector) + ] + expected: tuple[float, float] = (2.250, 0.606) + self.assertSequenceEqual(tuple(obtained), expected) + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsFunctionsGeosLogReader.py b/geos-posp/tests/testsFunctionsGeosLogReader.py new file mode 100644 index 00000000..1f3ac1a7 --- /dev/null +++ b/geos-posp/tests/testsFunctionsGeosLogReader.py @@ -0,0 +1,491 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import contextlib +import io +import os +import sys +import unittest + +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.processing import geosLogReaderFunctions as utils +from geos_posp.utils.enumUnits import Unit, getSIUnits + + +class TestsFunctionsGeosLogReader(unittest.TestCase): + def test_replaceSpecialCharactersWithWhitespace(self: Self) -> None: + """Test replaceSpecialCharactersWithWhitespace function.""" + example: str = "hi '(_there(''&*$^,:;'" + expected: str = "hi there " + obtained: str = utils.replaceSpecialCharactersWithWhitespace(example) + self.assertEqual(expected, obtained) + + def test_formatPropertyName(self: Self) -> None: + """Test formatPropertyName function.""" + example: str = " Delta pressure min" + expected: str = "DeltaPressureMin" + obtained: str = utils.formatPropertyName(example) + self.assertEqual(expected, obtained) + + def test_extractRegion(self: Self) -> None: + """Test extractRegion function.""" + example: str = ( + "Adding Object CellElementRegion named Reservoir from" + " ObjectManager::Catalog." + ) + expected: str = "Reservoir" + obtained: str = utils.extractRegion(example) + self.assertEqual(expected, obtained) + + def test_extractStatsName(self: Self) -> None: + """Test extractStatsName function.""" + example: str = ( + "compflowStatistics, Reservoir: Pressure (min, average, max): " + "2.86419e+07, 2.93341e+07, 3.006e+07 Pa" + ) + expected: str = "compflowStatistics" + obtained: str = utils.extractStatsName(example) + self.assertEqual(expected, obtained) + + def test_extractPhaseModel(self: Self) -> None: + """Test extractPhaseModel function.""" + example: str = ( + " TableFunction: " "fluid_phaseModel1_PhillipsBrineDensity_table" + ) + expected: str = "PhillipsBrineDensity" + obtained: str = utils.extractPhaseModel(example) + self.assertEqual(expected, obtained) + + def test_buildPropertiesNameForPhases(self: Self) -> None: + """Test buildPropertiesNameForPhases function.""" + example_block: str = " Mobile phase mass" + example_phases: list[str] = ["CO2", "Water"] + expected: list[str] = [" Mobile CO2 mass", " Mobile Water mass"] + obtained: list[str] = utils.buildPropertiesNameForPhases( + example_block, example_phases + ) + self.assertEqual(expected, obtained) + + def test_buildPropertiesNameForComponents(self: Self) -> None: + """Test buildPropertiesNameForComponents function.""" + example: list[str] = ["CO2", "Water"] + expected: list[str] = [ + "Dissolved mass CO2 in CO2", + "Dissolved mass Water in CO2", + "Dissolved mass CO2 in Water", + "Dissolved mass Water in Water", + ] + obtained: list[str] = utils.buildPropertiesNameForComponents(example) + self.assertEqual(expected, obtained) + + def test_buildPropertiesNameNoPhases(self: Self) -> None: + """Test buildPropertiesNameNoPhases function.""" + example_name_block: str = " Delta pressure " + example_extensions: str = "min, max)" + expected: list[str] = [" Delta pressure min", " Delta pressure max"] + obtained: list[str] = utils.buildPropertiesNameNoPhases( + example_name_block, example_extensions + ) + self.assertEqual(expected, obtained) + + def test_buildPropertiesNameNoPhases2(self: Self) -> None: + """Test buildPropertiesNameNoPhases function.""" + example: str = " Delta pressure " + expected: list[str] = [" Delta pressure "] + obtained: list[str] = utils.buildPropertiesNameNoPhases(example) + self.assertEqual(expected, obtained) + + def test_buildPropertiesNameFromGeosProperties(self: Self) -> None: + """Test buildPropertiesNameFromGeosProperties function.""" + examples_phases: list[str] = ["CO2", "Water"] + example: str = " Pressure (min, average, max)" + expected: list[str] = [" Pressure min", " Pressure average", " Pressure max"] + obtained: list[str] = utils.buildPropertiesNameFromGeosProperties( + example, examples_phases + ) + self.assertEqual(expected, obtained) + + example = " Total dynamic pore volume" + expected = [" Total dynamic pore volume"] + obtained = utils.buildPropertiesNameFromGeosProperties(example, examples_phases) + self.assertEqual(expected, obtained) + + example = " Non-trapped phase mass (metric 1)" + expected = [" Non-trapped CO2 mass ", " Non-trapped Water mass "] + obtained = utils.buildPropertiesNameFromGeosProperties(example, examples_phases) + self.assertEqual(expected, obtained) + + example = " Dissolved component mass" + expected = [ + "Dissolved mass CO2 in CO2", + "Dissolved mass Water in CO2", + "Dissolved mass CO2 in Water", + "Dissolved mass Water in Water", + ] + obtained = utils.buildPropertiesNameFromGeosProperties(example, examples_phases) + self.assertEqual(expected, obtained) + + example = " Component mass" + expected = [ + "Dissolved mass CO2 in CO2", + "Dissolved mass Water in CO2", + "Dissolved mass CO2 in Water", + "Dissolved mass Water in Water", + ] + obtained = utils.buildPropertiesNameFromGeosProperties(example, examples_phases) + self.assertEqual(expected, obtained) + + def test_extractPropertiesFlow(self: Self) -> None: + """Test extractPropertiesFlow function.""" + example_block: str = ( + "compflowStatistics, Reservoir: Trapped phase mass (metric 1):" + " { 0, 1.9147e+10 } kg" + ) + examples_phases: list[str] = ["CO2", "Water"] + expected: list[str] = [ + "Reservoir__TrappedCO2Mass", + "Reservoir__TrappedWaterMass", + ] + obtained: list[str] = utils.extractPropertiesFlow( + example_block, examples_phases + ) + self.assertEqual(expected, obtained) + + example_block = ( + "compflowStatistics, Reservoir: Phase mass:" " { 0, 1.01274e+14 } kg" + ) + expected = ["Reservoir__CO2Mass", "Reservoir__WaterMass"] + obtained = utils.extractPropertiesFlow(example_block, examples_phases) + self.assertEqual(expected, obtained) + + example_block = ( + "compflowStatistics, Region1 (time 4320000 s): Pressure" + " (min, average, max): 10984659.811871096, 11257138.433702637," + " 11535137.236653088 Pa" + ) + expected = [ + "Region1__PressureMin", + "Region1__PressureAverage", + "Region1__PressureMax", + ] + obtained = utils.extractPropertiesFlow(example_block, examples_phases) + self.assertEqual(expected, obtained) + + def test_countNumberLines(self: Self) -> None: + """Test countNumberLines function.""" + log1: str = os.path.join(dir_path, "Data/job_GEOS_825200.out") + expected1: int = 24307 + obtained1: int = utils.countNumberLines(log1) + self.assertEqual(expected1, obtained1) + + def test_extractValuesFlow(self: Self) -> None: + """Test extractValuesFlow function.""" + example: str = ( + "compflowStatistics, Reservoir: Pressure (min, average, max):" + " 1.25e+07, 1.25e+07, 1.25e+07 Pa" + ) + expected: list[float] = [1.25e07, 1.25e07, 1.25e07] + obtained: list[float] = utils.extractValuesFlow(example) + self.assertEqual(expected, obtained) + + example = ( + "compflowStatistics, Reservoir: Phase dynamic pore volumes:" + " { 0, 6.61331e+07 } rm^3" + ) + expected = [0.0, 6.61331e07] + obtained = utils.extractValuesFlow(example) + self.assertEqual(expected, obtained) + + example = ( + "compflowStatistics, Reservoir: Dissolved component mass:" + " { { 0, 0 }, { 0, 6.38235e+10 } } kg" + ) + expected = [0.0, 0.0, 0.0, 6.38235e10] + obtained = utils.extractValuesFlow(example) + self.assertEqual(expected, obtained) + + example = ( + "compflowStatistics, Reservoir: Cell fluid mass" + " (min, max): 10765.1, 2.2694e+10 kg" + ) + expected = [10765.1, 2.2694e10] + obtained = utils.extractValuesFlow(example) + self.assertEqual(expected, obtained) + + example = ( + "compflowStatistics, Region1 (time 256800000 s): Pressure" + " (min, average, max): 10023287.92961521, 10271543.591259222," + " 10525096.98374942 Pa" + ) + expected = [10023287.92961521, 10271543.591259222, 10525096.98374942] + obtained = utils.extractValuesFlow(example) + self.assertEqual(expected, obtained) + + example = ( + "compflowStatistics, Region1 (time 4320000 s): Phase dynamic" + " pore volume: [0, 799999924.1499865] rm^3" + ) + expected = [0, 799999924.1499865] + obtained = utils.extractValuesFlow(example) + self.assertEqual(expected, obtained) + + def test_convertValues(self: Self) -> None: + """Test convertValues function.""" + propertyNames: list[str] = [" Delta pressure min ", " CO2 volume "] + propertyValues: list[float] = [1e6, 2e8] + propertyUnits: dict[str, Unit] = getSIUnits() + expected: list[float] = [1e6, 2e8] + obtained: list[float] = utils.convertValues( + propertyNames, propertyValues, propertyUnits + ) + self.assertEqual(expected, obtained) + + propertyNames = ["WellControls__TotalFluidDensity"] + propertyValues = [1e4] + expected = [1e4] + obtained = utils.convertValues(propertyNames, propertyValues, propertyUnits) + self.assertEqual(expected, obtained) + + def test_extractWell(self: Self) -> None: + """Test extractWell function.""" + line = " TableFunction: well.CO2001_ConstantBHP_table" + expected = "well.CO2001" + obtained = utils.extractWell(line) + self.assertEqual(expected, obtained) + + def test_identifyCurrentWell(self: Self) -> None: + """Test identifyCurrentWell function.""" + lastWellName: str = "well1" + line: str = ( + "The total rate is 0 kg/s, which corresponds to a" + + "total surface volumetric rate of 0 sm3/s" + ) + expected: str = "well1" + obtained: str = utils.identifyCurrentWell(line, lastWellName) + self.assertEqual(expected, obtained) + + line = ( + "Rank 18: well.CO2001: BHP (at the specified reference" + + " elevation): 19318538.400682557 Pa" + ) + expected = "well.CO2001" + obtained = utils.identifyCurrentWell(line, lastWellName) + self.assertEqual(expected, obtained) + + line = ( + "wellControls1: BHP (at the specified reference" + + " elevation): 12337146.157562563 Pa" + ) + expected = "wellControls1" + obtained = utils.identifyCurrentWell(line, lastWellName) + self.assertEqual(expected, obtained) + + def test_extractWellTags(self: Self) -> None: + """Test extractWellTags function.""" + line: str = ( + "Rank 18: well.CO2001: BHP " + + "(at the specified reference elevation): 193000 Pa" + ) + expected: list[str] = ["BHP"] + obtained: list[str] = utils.extractWellTags(line) + self.assertEqual(expected, obtained) + + line = ( + "The total rate is 0 kg/s, which corresponds" + + " to a total surface volumetric rate of 0 sm3/s" + ) + expected = ["total massRate", "total surface volumetricRate"] + obtained = utils.extractWellTags(line) + self.assertEqual(expected, obtained) + + def test_extractValuesWell(self: Self) -> None: + """Test extractValuesWell function.""" + line: str = ( + "Rank 18: well.CO2001: BHP " + + "(at the specified reference elevation): 193000 Pa" + ) + expected: list[float] = [193000.0] + obtained: list[float] = utils.extractValuesWell(line, 1) + self.assertEqual(expected, obtained) + line = ( + "The total rate is 0 kg/s, which corresponds" + + " to a total surface volumetric rate of 0 sm3/s" + ) + expected = [0.0, 0.0] + obtained = utils.extractValuesWell(line, 2) + self.assertEqual(expected, obtained) + + line = "The phase surface volumetric rate is" + " 1.9466968733035026e-12 sm3/s" + expected = [1.9466968733035026e-12] + obtained = utils.extractValuesWell(line, 1) + self.assertEqual(expected, obtained) + + def test_extractAquifer(self: Self) -> None: + """Test extractAquifer function.""" + line: str = " TableFunction:aquifer1_pressureInfluence_table" + expected: str = "aquifer1" + obtained: str = utils.extractAquifer(line) + self.assertEqual(expected, obtained) + + def test_extractValueAndNameAquifer(self: Self) -> None: + """Test extractValueAndNameAquifer function.""" + line: str = ( + "FlowSolverBase compositionalMultiphaseFlow" + + " (SimuDeck_aquifer_pression_meme.xml, l.28): at time 100s, the" + + " boundary condition 'aquifer1' produces a flux of" + + " -0.6181975187076816 kg (or moles if useMass=0)." + ) + expected: tuple[str, float] = ("aquifer1", -0.6181975187076816) + obtained: tuple[str, float] = utils.extractValueAndNameAquifer(line) + self.assertEqual(expected, obtained) + + line = ( + "FlowSolverBase compositionalMultiphaseFVMSolver" + + " (nl_multiphase_with_well_reservoir_homo_for_Pierre_versionPaul" + + "_hysteresisIX.xml, l.31): at time 25636.406820617773s, the" + + " boundary condition 'Aquifer3' produces a flux of" + + " -0.8441759009606705 kg (or moles if useMass=0). " + ) + expected = ("Aquifer3", -0.8441759009606705) + obtained = utils.extractValueAndNameAquifer(line) + self.assertEqual(expected, obtained) + + def test_extractNewtonIter(self: Self) -> None: + """Test extractNewtonIter function.""" + line: str = " Attempt: 2, ConfigurationIter: 1, NewtonIter: 8" + expected: int = 8 + obtained: int = utils.extractNewtonIter(line) + self.assertEqual(expected, obtained) + + def test_extractLinearIter(self: Self) -> None: + """Test extractLinearIter function.""" + line: str = ( + " Linear Solver | Success | Iterations: 23 | Final Rel Res:" + + " 5.96636e-05 | Make Restrictor Time: 0 | Compute Auu Time: 0 |" + + " SC Filter Time: 0 | Setup Time: 1.5156 s | Solve Time:" + + " 0.041093 s" + ) + expected: int = 23 + obtained: int = utils.extractLinearIter(line) + self.assertEqual(expected, obtained) + + def test_timeInSecond(self: Self) -> None: + """Test timeInSecond function.""" + timeCounter: dict[str, float] = { + "years": 0, + "days": 0, + "hrs": 0, + "min": 0, + "s": 0, + } + expected: float = 0.0 + obtained: float = utils.timeInSecond(timeCounter) + self.assertEqual(expected, obtained) + + timeCounter = {"years": 1, "days": 1, "hrs": 1, "min": 1, "s": 1} + expected = 31647661.0 + obtained = utils.timeInSecond(timeCounter) + self.assertEqual(expected, obtained) + + def test_extractTimeAndDt(self: Self) -> None: + """Test extractTimeAndDt function.""" + line: str = "Time: 1 s, dt: 1 s, Cycle: 0" + expected: tuple[float, float] = (1.0, 1.0) + obtained: tuple[float, float] = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + line = "Time: 1s, dt: 1s, Cycle: 0" + expected = (1.0, 1.0) + obtained = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + line = "Time: 1e5s, dt: 1e6s, Cycle: 0" + expected = (1.0e5, 1.0e6) + obtained = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + line = "Time: 1 min, dt: 1 s, Cycle: 0" + expected = (60.0, 1.0) + obtained = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + line = "Time: 1 hrs, dt: 1 s, Cycle: 0" + expected = (3600.0, 1.0) + obtained = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + line = "Time: 1 days, dt: 1 s, Cycle: 0" + expected = (86400.0, 1.0) + obtained = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + line = "Time: 1 years, 1 days, 1 hrs, 1 min, 1 s, dt: 1 s, Cycle: 1" + expected = (31647661.0, 1.0) + obtained = utils.extractTimeAndDt(line) + self.assertEqual(expected, obtained) + + def test_identifyProperties(self: Self) -> None: + """Test identifyProperties function.""" + properties: list[str] = ["WellControls_TotalFluidDensity"] + expected: list[str] = ["35:WellControls_TotalFluidDensity"] + obtained: list[str] = utils.identifyProperties(properties) + self.assertEqual(expected, obtained) + + def test_findNumberPhasesSimulation(self: Self) -> None: + """Test findNumberPhasesSimulation function.""" + filename: str = "job_GEOS_825200.out" + pathToFile: str = os.path.join(dir_path, "Data/") + filepath: str = os.path.join(pathToFile, filename) + expected: int = 2 + obtained: int = utils.findNumberPhasesSimulation(filepath) + self.assertEqual(expected, obtained) + + def test_transformUserChoiceToListPhases(self: Self) -> None: + """Test phaseNameBuilder function with 3 phases.""" + userChoice: str = "phase0 phase1 phase2" + expected: list[str] = ["phase0", "phase1", "phase2"] + obtained: list[str] = utils.transformUserChoiceToListPhases(userChoice) + self.assertEqual(expected, obtained) + + userChoice = "phase0, phase1, phase2" + expected = ["phase0", "phase1", "phase2"] + obtained = utils.transformUserChoiceToListPhases(userChoice) + self.assertEqual(expected, obtained) + + userChoice = "phase0; phase1; phase2" + expected = [] + capturedOutput = io.StringIO() + with contextlib.redirect_stdout(capturedOutput): + obtained = utils.transformUserChoiceToListPhases(userChoice) + self.assertEqual(expected, obtained) + self.assertGreater(len(capturedOutput.getvalue()), 0) + + def test_phaseNamesBuilder(self: Self) -> None: + """Test phaseNameBuilder function with 4 phases.""" + phasesFromUser: list[str] = [] + expected: list[str] = ["phase0", "phase1", "phase2", "phase3"] + obtained: list[str] = utils.phaseNamesBuilder(4, phasesFromUser) + self.assertEqual(expected, obtained) + + phasesFromUser = ["water", "gas"] + expected = ["water", "gas", "phase2", "phase3"] + obtained = utils.phaseNamesBuilder(4, phasesFromUser) + self.assertEqual(expected, obtained) + + phasesFromUser = ["water", "CO2", "N2", "H2", "CH4"] + expected = ["water", "CO2", "N2", "H2"] + obtained = utils.phaseNamesBuilder(4, phasesFromUser) + self.assertEqual(expected, obtained) + + # TODO def test_extractValuesFromBlockWhenMultipleComponents(self :Self) + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsFunctionsGeosUtils.py b/geos-posp/tests/testsFunctionsGeosUtils.py new file mode 100644 index 00000000..7de59de6 --- /dev/null +++ b/geos-posp/tests/testsFunctionsGeosUtils.py @@ -0,0 +1,34 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto, Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import geos_posp.utils.geosUtils as fcts + +matrix: npt.NDArray[np.float64] = np.array([[11, 21, 31], [21, 22, 23], [31, 23, 33]]) +vector: npt.NDArray[np.float64] = np.array([11, 22, 33, 23, 31, 21]) + + +class TestsFunctionsGeosUtils(unittest.TestCase): + + def test_getAttributeMatrixFromVector(self: Self) -> None: + """Test conversion from Matrix to Vector for Geos stress.""" + obtained: npt.NDArray[np.float64] = fcts.getAttributeMatrixFromVector(vector) + self.assertTrue(np.all(np.equal(obtained, matrix))) + + def test_getAttributeVectorFromMatrix(self: Self) -> None: + """Test conversion from Vector to Matrix for Geos stress.""" + obtained: npt.NDArray[np.float64] = fcts.getAttributeVectorFromMatrix(matrix, 6) + self.assertTrue(np.all(np.equal(obtained, vector))) diff --git a/geos-posp/tests/testsGeometryFunctions.py b/geos-posp/tests/testsGeometryFunctions.py new file mode 100644 index 00000000..3f7ddb0b --- /dev/null +++ b/geos-posp/tests/testsGeometryFunctions.py @@ -0,0 +1,172 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import geos_posp.processing.geometryFunctions as fcts + +basisCanon: tuple[ + npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64] +] = (np.array([1.0, 0.0, 0.0]), np.array([0.0, 1.0, 0.0]), np.array([0.0, 0.0, 1.0])) +# destination basis according to canonic coordinates +basisTo0: tuple[ + npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64] +] = (np.array([2.0, 3.0, 0.0]), np.array([4.0, 5.0, 0.0]), np.array([0.0, 0.0, 1.0])) +basisTo1: tuple[ + npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64] +] = (np.array([1.0, 1.0, 0.0]), np.array([0.0, 1.0, 1.0]), np.array([1.0, 0.0, 1.0])) +basisTo2: tuple[ + npt.NDArray[np.float64], npt.NDArray[np.float64], npt.NDArray[np.float64] +] = (np.array([0.0, 2.0, 0.0]), np.array([-2.0, 0.0, 0.0]), np.array([0.0, 0.0, 2.0])) + + +class TestsGeometryFunctions(unittest.TestCase): + def test_getChangeOfBasisMatrixToCanonic(self: Self) -> None: + """Test change of basis matrix using canonic basis.""" + obtained: npt.NDArray[np.float64] = fcts.getChangeOfBasisMatrix( + basisTo0, basisCanon + ) + # matrix where the columns are the vectors + expected: npt.NDArray[np.float64] = np.transpose(np.array(basisTo0)) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_getChangeOfBasisMatrix(self: Self) -> None: + """Test change of basis matrix format from basis vectors.""" + obtained: npt.NDArray[np.float64] = fcts.getChangeOfBasisMatrix( + basisTo0, basisTo1 + ) + expected: npt.NDArray[np.float64] = np.array( + [[2.5, 4.5, -0.5], [0.5, 0.5, 0.5], [-0.5, -0.5, 0.5]] + ) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_computeCoordinatesInNewBasisIdentity(self: Self) -> None: + """Test calculation of coordinates of a vector in the same basis.""" + vec: npt.NDArray[np.float64] = np.array([2.0, 3.0, 4.0]) + + # get change of basis matrix + changeOfBasisMatrix: npt.NDArray[np.float64] = fcts.getChangeOfBasisMatrix( + basisCanon, basisCanon + ) + obtained: npt.NDArray[np.float64] = fcts.computeCoordinatesInNewBasis( + vec, changeOfBasisMatrix + ) + expected: npt.NDArray[np.float64] = vec + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_computeCoordinatesInNewBasis(self: Self) -> None: + """Test calculation of coordinates of a vector in another basis.""" + vec: npt.NDArray[np.float64] = np.array([2.0, 3.0, 4.0]) + + # get change of basis matrix and the inverse + changeOfBasisMatrix: npt.NDArray[np.float64] = fcts.getChangeOfBasisMatrix( + basisTo0, basisTo1 + ) + obtained = fcts.computeCoordinatesInNewBasis(vec, changeOfBasisMatrix) + expected: npt.NDArray[np.float64] = np.array([16.5, 4.5, -0.5]) + self.assertTrue( + np.array_equal(np.round(obtained, 2), np.round(expected, 2), equal_nan=True) + ) + + def test_computePlaneFrom3Points(self: Self) -> None: + """Test calculation of plane coefficients from 3 points.""" + pt1: npt.NDArray[np.float64] = np.array([1.0, 2.0, 1.0]) + pt2: npt.NDArray[np.float64] = np.array([1.0, 1.0, 2.0]) + pt3: npt.NDArray[np.float64] = np.array([3.0, 2.0, 2.0]) + obtained: tuple[float, float, float, float] = fcts.computePlaneFrom3Points( + pt1, pt2, pt3 + ) + expected: tuple[float, float, float, float] = (-1.0, 2.0, 2.0, -5.0) + self.assertSequenceEqual(obtained, expected) + + def test_getPointSideAgainstPlaneAssertion(self: Self) -> None: + """Test get point side against a plane.""" + planePt: npt.NDArray[np.float64] = np.array([0.0, 0.0, 0.0]) + + # assertion error - Point on the plane + planeNormal: npt.NDArray[np.float64] = np.array([0.0, 0.0, 1.0]) + self.assertRaises( + AssertionError, fcts.getPointSideAgainstPlane, planePt, planePt, planeNormal + ) + + def test_getPointSideAgainstPlaneHorizontal(self: Self) -> None: + """Test get point side against a horizontal plane.""" + # horizontal plane + planePt: npt.NDArray[np.float64] = np.array([0.0, 0.0, 0.0]) + listPtsCoords: list[npt.NDArray[np.float64]] = [ + np.array([0.5, 0.5, 0.5]), + np.array([0.5, 0.5, -0.5]), + ] + planeNormal: npt.NDArray[np.float64] = np.array([0.0, 0.0, 1.0]) + obtained: list[bool] = [] + for ptCoords in listPtsCoords: + side: bool = fcts.getPointSideAgainstPlane(ptCoords, planePt, planeNormal) + obtained += [side] + expected: tuple[bool, bool] = (True, False) + self.assertSequenceEqual(obtained, expected) + + def test_getPointSideAgainstPlaneVertical(self: Self) -> None: + """Test get point side against a vertical plane.""" + # vertical plane + planePt: npt.NDArray[np.float64] = np.array([0.0, 0.0, 0.0]) + listPtsCoords: list[npt.NDArray[np.float64]] = [ + np.array([0.5, 0.5, 0.5]), + np.array([-0.5, 0.5, 0.5]), + ] + planeNormal: npt.NDArray[np.float64] = np.array([1.0, 0.0, 0.0]) + obtained: list[bool] = [] + for ptCoords in listPtsCoords: + side: bool = fcts.getPointSideAgainstPlane(ptCoords, planePt, planeNormal) + obtained += [side] + expected: tuple[bool, bool] = (True, False) + self.assertSequenceEqual(obtained, expected) + + def test_getCellSideAgainstPlaneRandom(self: Self) -> None: + """Test get cell side against a plane.""" + # random plane + planePt = np.array([125.58337, 1386.0465, -2782.502]) + listCellPtsCoords = [ + np.array( + [ + [135.49551, 1374.7644, -2786.884], + [125.58337, 1376.7441, -2782.502], + [132.19525, 1382.2516, -2771.0508], + [125.58337, 1386.0465, -2782.502], + ] + ), + np.array( + [ + [111.9148, 1377.0265, -2764.875], + [132.19525, 1382.2516, -2771.0508], + [125.58337, 1376.7441, -2782.502], + [125.58337, 1386.0465, -2782.502], + ] + ), + ] + planeNormal = np.array([0.8660075, 0.0, -0.5000311]) + obtained = [] + for cellPtsCoords in listCellPtsCoords: + side: bool = fcts.getCellSideAgainstPlane( + cellPtsCoords, planePt, planeNormal + ) + obtained += [side] + expected = (True, False) + self.assertSequenceEqual(obtained, expected) diff --git a/geos-posp/tests/testsGeosLogReaderConvergence.py b/geos-posp/tests/testsGeosLogReaderConvergence.py new file mode 100644 index 00000000..b3d8e7ed --- /dev/null +++ b/geos-posp/tests/testsGeosLogReaderConvergence.py @@ -0,0 +1,71 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.readers.GeosLogReaderConvergence import GeosLogReaderConvergence +from geos_posp.utils.UnitRepository import Unit, UnitRepository + +unitsObjSI: UnitRepository = UnitRepository() +conversionFactors: dict[str, Unit] = unitsObjSI.getPropertiesUnit() +pathFlowSim: str = os.path.join(dir_path, "Data/small_job_GEOS_246861.out") + + +class TestsFunctionsGeosLogReaderConvergence(unittest.TestCase): + def test1_readAllSimulation(self: Self) -> None: + """Test convergence reader.""" + obj: GeosLogReaderConvergence = GeosLogReaderConvergence( + pathFlowSim, conversionFactors + ) + expectedPropertiesValues = { + "23:NewtonIter": [1, 1, 1], + "24:LinearIter": [1, 2, 2], + "23:CumulatedNewtonIter": [1, 2, 3], + "24:CumulatedLinearIter": [1, 3, 5], + } + self.assertEqual( + list(obj.m_solversIterationsValues.keys()), + list(expectedPropertiesValues.keys()), + ) + self.assertEqual(obj.m_solversIterationsValues, expectedPropertiesValues) + expectedTimesteps: list[float] = [0.0, 8600.0, 25724.3] + self.assertEqual(obj.m_timesteps, expectedTimesteps) + expectedDts: list[float] = [8600.0, 17124.3, 34165.3] + self.assertEqual(obj.m_dts, expectedDts) + expectedDF: pd.DataFrame = pd.DataFrame() + columns_name = [ + "23:NewtonIter", + "24:LinearIter", + "23:CumulatedNewtonIter", + "24:CumulatedLinearIter", + "Time__s", + "dt__s", + ] + values: list[list[float]] = [ + [1.0, 1.0, 1.0], + [1.0, 2.0, 2.0], + [1.0, 2.0, 3.0], + [1.0, 3.0, 5.0], + [0.0, 8600.0, 25724.3], + [8600.0, 17124.3, 34165.3], + ] + for column_name, value in zip(columns_name, values): + expectedDF[column_name] = value + obtainedDF: pd.DataFrame = obj.createDataframe() + self.assertEqual(list(obtainedDF.columns), columns_name) + self.assertTrue(expectedDF.equals(obtainedDF)) + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsGeosLogReaderFlow.py b/geos-posp/tests/testsGeosLogReaderFlow.py new file mode 100644 index 00000000..f8749fc9 --- /dev/null +++ b/geos-posp/tests/testsGeosLogReaderFlow.py @@ -0,0 +1,248 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import contextlib +import io +import os +import sys +import unittest + +import pandas as pd # type: ignore[import-untyped] +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.readers.GeosLogReaderFlow import GeosLogReaderFlow +from geos_posp.utils.UnitRepository import Unit, UnitRepository + +unitsObjSI: UnitRepository = UnitRepository() +conversionFactors: dict[str, Unit] = unitsObjSI.getPropertiesUnit() +pathFlowSim: str = os.path.join(dir_path, "Data/job_GEOS_825200.out") +pathFlowSim2: str = os.path.join(dir_path, "Data/small_job_GEOS_825200.out") +pathFlowSim8: str = os.path.join( + dir_path, "Data/depleted_gas_reservoir_newwell_report.out" +) + + +class TestsFunctionsGeosLogReader(unittest.TestCase): + + def test0_regionsPropertiesKeysSimulation1(self: Self) -> None: + """Test case 2 phases, 5 regions, for time steps.""" + obj: GeosLogReaderFlow = GeosLogReaderFlow( + pathFlowSim, conversionFactors, ["CO2", "water"] + ) + self.assertEqual( + obj.m_regionNames, + ["Reservoir", "Caprock", "Overburden", "Underburden", "Salt"], + ) + self.assertEqual(obj.m_computeStatisticsName, "compflowStatistics") + self.assertEqual(obj.m_phaseNames, ["CO2", "water"]) + expected: list[str] = [ + "1:Reservoir__PressureMin", + "1:Reservoir__PressureAverage", + "1:Reservoir__PressureMax", + "0:Reservoir__DeltaPressureMin", + "0:Reservoir__DeltaPressureMax", + "2:Reservoir__TemperatureMin", + "2:Reservoir__TemperatureAverage", + "2:Reservoir__TemperatureMax", + "3:Reservoir__TotalDynamicPoreVolume", + "4:Reservoir__CO2DynamicPoreVolumes", + "4:Reservoir__WaterDynamicPoreVolumes", + "10:Reservoir__CO2Mass", + "10:Reservoir__WaterMass", + "6:Reservoir__TrappedCO2Mass", + "6:Reservoir__TrappedWaterMass", + "5:Reservoir__NonTrappedCO2Mass", + "5:Reservoir__NonTrappedWaterMass", + "7:Reservoir__ImmobileCO2Mass", + "7:Reservoir__ImmobileWaterMass", + "8:Reservoir__MobileCO2Mass", + "8:Reservoir__MobileWaterMass", + "9:Reservoir__DissolvedMassCO2InCO2", + "9:Reservoir__DissolvedMassWaterInCO2", + "9:Reservoir__DissolvedMassCO2InWater", + "9:Reservoir__DissolvedMassWaterInWater", + "1:Caprock__PressureMin", + "1:Caprock__PressureAverage", + "1:Caprock__PressureMax", + "0:Caprock__DeltaPressureMin", + "0:Caprock__DeltaPressureMax", + "2:Caprock__TemperatureMin", + "2:Caprock__TemperatureAverage", + "2:Caprock__TemperatureMax", + "3:Caprock__TotalDynamicPoreVolume", + "4:Caprock__CO2DynamicPoreVolumes", + "4:Caprock__WaterDynamicPoreVolumes", + "10:Caprock__CO2Mass", + "10:Caprock__WaterMass", + "6:Caprock__TrappedCO2Mass", + "6:Caprock__TrappedWaterMass", + "5:Caprock__NonTrappedCO2Mass", + "5:Caprock__NonTrappedWaterMass", + "7:Caprock__ImmobileCO2Mass", + "7:Caprock__ImmobileWaterMass", + "8:Caprock__MobileCO2Mass", + "8:Caprock__MobileWaterMass", + "9:Caprock__DissolvedMassCO2InCO2", + "9:Caprock__DissolvedMassWaterInCO2", + "9:Caprock__DissolvedMassCO2InWater", + "9:Caprock__DissolvedMassWaterInWater", + "1:Overburden__PressureMin", + "1:Overburden__PressureAverage", + "1:Overburden__PressureMax", + "0:Overburden__DeltaPressureMin", + "0:Overburden__DeltaPressureMax", + "2:Overburden__TemperatureMin", + "2:Overburden__TemperatureAverage", + "2:Overburden__TemperatureMax", + "3:Overburden__TotalDynamicPoreVolume", + "4:Overburden__CO2DynamicPoreVolumes", + "4:Overburden__WaterDynamicPoreVolumes", + "10:Overburden__CO2Mass", + "10:Overburden__WaterMass", + "6:Overburden__TrappedCO2Mass", + "6:Overburden__TrappedWaterMass", + "5:Overburden__NonTrappedCO2Mass", + "5:Overburden__NonTrappedWaterMass", + "7:Overburden__ImmobileCO2Mass", + "7:Overburden__ImmobileWaterMass", + "8:Overburden__MobileCO2Mass", + "8:Overburden__MobileWaterMass", + "9:Overburden__DissolvedMassCO2InCO2", + "9:Overburden__DissolvedMassWaterInCO2", + "9:Overburden__DissolvedMassCO2InWater", + "9:Overburden__DissolvedMassWaterInWater", + "1:Underburden__PressureMin", + "1:Underburden__PressureAverage", + "1:Underburden__PressureMax", + "0:Underburden__DeltaPressureMin", + "0:Underburden__DeltaPressureMax", + "2:Underburden__TemperatureMin", + "2:Underburden__TemperatureAverage", + "2:Underburden__TemperatureMax", + "3:Underburden__TotalDynamicPoreVolume", + "4:Underburden__CO2DynamicPoreVolumes", + "4:Underburden__WaterDynamicPoreVolumes", + "10:Underburden__CO2Mass", + "10:Underburden__WaterMass", + "6:Underburden__TrappedCO2Mass", + "6:Underburden__TrappedWaterMass", + "5:Underburden__NonTrappedCO2Mass", + "5:Underburden__NonTrappedWaterMass", + "7:Underburden__ImmobileCO2Mass", + "7:Underburden__ImmobileWaterMass", + "8:Underburden__MobileCO2Mass", + "8:Underburden__MobileWaterMass", + "9:Underburden__DissolvedMassCO2InCO2", + "9:Underburden__DissolvedMassWaterInCO2", + "9:Underburden__DissolvedMassCO2InWater", + "9:Underburden__DissolvedMassWaterInWater", + "1:Salt__PressureMin", + "1:Salt__PressureAverage", + "1:Salt__PressureMax", + "0:Salt__DeltaPressureMin", + "0:Salt__DeltaPressureMax", + "2:Salt__TemperatureMin", + "2:Salt__TemperatureAverage", + "2:Salt__TemperatureMax", + "3:Salt__TotalDynamicPoreVolume", + "4:Salt__CO2DynamicPoreVolumes", + "4:Salt__WaterDynamicPoreVolumes", + "10:Salt__CO2Mass", + "10:Salt__WaterMass", + "6:Salt__TrappedCO2Mass", + "6:Salt__TrappedWaterMass", + "5:Salt__NonTrappedCO2Mass", + "5:Salt__NonTrappedWaterMass", + "7:Salt__ImmobileCO2Mass", + "7:Salt__ImmobileWaterMass", + "8:Salt__MobileCO2Mass", + "8:Salt__MobileWaterMass", + "9:Salt__DissolvedMassCO2InCO2", + "9:Salt__DissolvedMassWaterInCO2", + "9:Salt__DissolvedMassCO2InWater", + "9:Salt__DissolvedMassWaterInWater", + ] + obtained: list[str] = list(obj.m_regionsPropertiesValues.keys()) + self.assertEqual(expected, obtained) + expectedTimesteps: list[float] = [ + 0.0, + 3.1536e07, + 6.3072e07, + 9.4608e07, + 1.26144e08, + 1.5768e08, + 1.89216e08, + 2.20752e08, + 2.52288e08, + 2.83824e08, + 3.1536e08, + 3.46896e08, + 3.78432e08, + 4.09968e08, + 4.41504e08, + 4.7304e08, + ] + self.assertEqual(obj.m_timesteps, expectedTimesteps) + + def test1_readAllSimulation2(self: Self) -> None: + """Test case 2 phases, 2 regions, for time steps.""" + obj: GeosLogReaderFlow = GeosLogReaderFlow( + pathFlowSim2, conversionFactors, ["CO2", "water"] + ) + self.assertEqual(obj.m_regionNames, ["Reservoir", "Caprock"]) + self.assertEqual(obj.m_phaseNames, ["CO2", "water"]) + self.assertEqual(obj.m_computeStatisticsName, "compflowStatistics") + regionPropertiesValuesExpected: dict[str, list[float]] = { + "1:Reservoir__PressureMin": [1.25e07, 2.80948e07], + "1:Reservoir__PressureAverage": [1.25e07, 2.99421e07], + "1:Reservoir__PressureMax": [1.25e07, 3.12538e07], + "8:Reservoir__MobileCO2Mass": [0.0, 1.3012e07], + "8:Reservoir__MobileWaterMass": [6.38235e10, 6.51497e10], + "1:Caprock__PressureMin": [1.25e07, 2.76478e07], + "1:Caprock__PressureAverage": [1.25e07, 2.89944e07], + "1:Caprock__PressureMax": [1.25e07, 2.98486e07], + "8:Caprock__MobileCO2Mass": [0.0, 2.19936e07], + "8:Caprock__MobileWaterMass": [1.25037e10, 1.27238e10], + } + self.assertEqual(obj.m_regionsPropertiesValues, regionPropertiesValuesExpected) + expectedTimesteps: list[float] = [0.0, 3.1536e07] + self.assertEqual(obj.m_timesteps, expectedTimesteps) + + def test2_DataframeFlowSimulation2(self: Self) -> None: + """Test case 2 phases, 2 regions, for dataframe creation.""" + obj: GeosLogReaderFlow = GeosLogReaderFlow( + pathFlowSim2, conversionFactors, ["CO2", "water"] + ) + data: dict[str, list[float]] = { + "1:Reservoir__PressureMin__Pa": [1.25e07, 2.80948e07], + "1:Reservoir__PressureAverage__Pa": [1.25e07, 2.99421e07], + "1:Reservoir__PressureMax__Pa": [1.25e07, 3.12538e07], + "8:Reservoir__MobileCO2Mass__kg": [0.0, 1.3012e07], + "8:Reservoir__MobileWaterMass__kg": [6.38235e10, 6.51497e10], + "1:Caprock__PressureMin__Pa": [1.25e07, 2.76478e07], + "1:Caprock__PressureAverage__Pa": [1.25e07, 2.89944e07], + "1:Caprock__PressureMax__Pa": [1.25e07, 2.98486e07], + "8:Caprock__MobileCO2Mass__kg": [0.0, 2.19936e07], + "8:Caprock__MobileWaterMass__kg": [1.25037e10, 1.27238e10], + "Time__s": [0.0, 3.1536e07], + } + expected: pd.DataFrame = pd.DataFrame(data) + obtained: pd.DataFrame = obj.createDataframe() + self.assertTrue(expected.equals(obtained)) + + def test_depleted_gas_reservoir_newwell_report(self: Self) -> None: + """Test case dt is missing.""" + obj: GeosLogReaderFlow = GeosLogReaderFlow(pathFlowSim8, conversionFactors) + self.assertEqual(obj.m_regionNames, ["Region1"]) + self.assertEqual(obj.m_phaseNames, ["phase0", "phase1"]) + self.assertEqual(obj.m_computeStatisticsName, "compflowStatistics") + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsGeosLogReaderWells.py b/geos-posp/tests/testsGeosLogReaderWells.py new file mode 100644 index 00000000..ba8c3113 --- /dev/null +++ b/geos-posp/tests/testsGeosLogReaderWells.py @@ -0,0 +1,236 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import contextlib +import io +import os +import sys +import unittest + +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +import pandas as pd # type: ignore[import-untyped] + +from geos_posp.readers.GeosLogReaderWells import GeosLogReaderWells +from geos_posp.utils.UnitRepository import Unit, UnitRepository + +unitsObjSI = UnitRepository() +conversionFactors: dict[str, Unit] = unitsObjSI.getPropertiesUnit() +pathFlowSim2: str = os.path.join(dir_path, "Data/small_job_GEOS_825200_wells.out") +pathFlowSim3: str = os.path.join(dir_path, "Data/runsinglephase.txt") +pathFlowSim4: str = os.path.join(dir_path, "Data/small_job_GEOS_891567.out") +pathFlowSim5: str = os.path.join(dir_path, "Data/job_GEOS_935933.out") + + +class TestsGeosLogReaderWells(unittest.TestCase): + def test1_readAllSimulation2(self: Self) -> None: + """Test reading wells with 3 wells and 2 phases.""" + obj: GeosLogReaderWells = GeosLogReaderWells( + pathFlowSim2, conversionFactors, ["CO2", "water"], 3 + ) + self.assertEqual(obj.m_phaseNames, ["CO2", "water"]) + self.assertEqual( + obj.m_wellNames, ["wellControls1", "wellControls2", "wellControls3"] + ) + expectedPropertiesValues = { + "11:WellControls1__BHP": [12337146.157562563, 27252686.916117527], + "12:WellControls1__TotalMassRate": [56.37348443784919, 56.32837354192296], + "13:WellControls1__TotalSurfaceVolumetricRate": [30.024025669350802, 30], + "14:WellControls1__SurfaceVolumetricRateCO2": [ + 30.023748128796043, + 29.9997226815373, + ], + "14:WellControls1__SurfaceVolumetricRateWater": [ + 0.00027754055475897704, + 0.00027731846270264625, + ], + "11:WellControls2__BHP": [13268440.020500632, 27450836.07294756], + "12:WellControls2__TotalMassRate": [56.38455514210006, 56.32837354192296], + "13:WellControls2__TotalSurfaceVolumetricRate": [30.029921829787227, 30], + "14:WellControls2__SurfaceVolumetricRateCO2": [ + 30.029644234728664, + 29.9997226815373, + ], + "14:WellControls2__SurfaceVolumetricRateWater": [ + 0.0002775950585639181, + 0.00027731846270264126, + ], + "11:WellControls3__BHP": [12318458.650753867, 26935804.208137162], + "12:WellControls3__TotalMassRate": [56.379144772078966, 56.32837354192296], + "13:WellControls3__TotalSurfaceVolumetricRate": [30.027040313946728, 30], + "14:WellControls3__SurfaceVolumetricRateCO2": [ + 30.02676274552475, + 29.9997226815373, + ], + "14:WellControls3__SurfaceVolumetricRateWater": [ + 0.0002775684219790799, + 0.00027731846270264625, + ], + "15:MeanBHP": [12641348.276272355, 27213109.065734085], + "16:MeanTotalMassRate": [56.37906145067607, 56.32837354192296], + "17:MeanTotalVolumetricRate": [30.02699593769492, 30], + "18:MeanSurfaceVolumetricRateCO2": [30.026718369683152, 29.999722681537303], + "18:MeanSurfaceVolumetricRateWater": [ + 0.00027756801176732497, + 0.00027731846270264457, + ], + } + self.assertEqual( + list(obj.m_wellsPropertiesValues.keys()), + list(expectedPropertiesValues.keys()), + ) + self.assertEqual(obj.m_wellsPropertiesValues, expectedPropertiesValues) + expectedTimesteps: list[float] = [0.0, 3.1536e07] + self.assertEqual(obj.m_timesteps, expectedTimesteps) + expectedDF: pd.DataFrame = pd.DataFrame() + columns_name = [ + "11:WellControls1__BHP__Pa", + "12:WellControls1__TotalMassRate__kg/s", + "13:WellControls1__TotalSurfaceVolumetricRate__m3/s", + "14:WellControls1__SurfaceVolumetricRateCO2__m3/s", + "14:WellControls1__SurfaceVolumetricRateWater__m3/s", + "11:WellControls2__BHP__Pa", + "12:WellControls2__TotalMassRate__kg/s", + "13:WellControls2__TotalSurfaceVolumetricRate__m3/s", + "14:WellControls2__SurfaceVolumetricRateCO2__m3/s", + "14:WellControls2__SurfaceVolumetricRateWater__m3/s", + "11:WellControls3__BHP__Pa", + "12:WellControls3__TotalMassRate__kg/s", + "13:WellControls3__TotalSurfaceVolumetricRate__m3/s", + "14:WellControls3__SurfaceVolumetricRateCO2__m3/s", + "14:WellControls3__SurfaceVolumetricRateWater__m3/s", + "15:MeanBHP__Pa", + "16:MeanTotalMassRate__kg/s", + "17:MeanTotalVolumetricRate__m3/s", + "18:MeanSurfaceVolumetricRateCO2__m3/s", + "18:MeanSurfaceVolumetricRateWater__m3/s", + "Time__s", + ] + values = [ + [12337146.157562563, 27252686.916117527], + [56.37348443784919, 56.32837354192296], + [30.024025669350802, 30], + [30.023748128796043, 29.9997226815373], + [0.00027754055475897704, 0.00027731846270264625], + [13268440.020500632, 27450836.07294756], + [56.38455514210006, 56.32837354192296], + [30.029921829787227, 30], + [30.029644234728664, 29.9997226815373], + [0.0002775950585639181, 0.00027731846270264126], + [12318458.650753867, 26935804.208137162], + [56.379144772078966, 56.32837354192296], + [30.027040313946728, 30], + [30.02676274552475, 29.9997226815373], + [0.0002775684219790799, 0.00027731846270264625], + [12641348.276272355, 27213109.065734085], + [56.37906145067607, 56.32837354192296], + [30.02699593769492, 30], + [30.026718369683152, 29.999722681537303], + [0.00027756801176732497, 0.00027731846270264457], + [0.0, 3.1536e07], + ] + for column_name, value in zip(columns_name, values): + expectedDF[column_name] = value + obtainedDF: pd.DataFrame = obj.createDataframe() + self.assertEqual(list(obtainedDF.columns), columns_name) + self.assertTrue(expectedDF.equals(obtainedDF)) + + def test3_readAllSimulation4(self: Self) -> None: + """Test reading wells with 1 well and 2 phases.""" + obj: GeosLogReaderWells = GeosLogReaderWells( + pathFlowSim4, conversionFactors, ["CO2", "water"], 1 + ) + self.assertEqual(obj.m_phaseNames, ["CO2", "water"]) + self.assertEqual(obj.m_wellNames, ["well_1Control"]) + expectedPropertiesValues = { + "11:Well1Control__BHP": [23960094.51907003, 23318529.329811733], + "12:Well1Control__TotalMassRate": [ + 0.00029566997749602594, + 0.00029566997749602507, + ], + "13:Well1Control__TotalSurfaceVolumetricRate": [ + 2.0000000000000063e-05, + 2e-05, + ], + "14:Well1Control__SurfaceVolumetricRateCO2": [ + 1.9999999999987377e-05, + 1.999999999998732e-05, + ], + "14:Well1Control__SurfaceVolumetricRateWater": [ + 1.2681312543855673e-17, + 1.2681312543888312e-17, + ], + "15:MeanBHP": [23960094.51907003, 23318529.329811733], + "16:MeanTotalMassRate": [0.00029566997749602594, 0.00029566997749602507], + "17:MeanTotalVolumetricRate": [2.0000000000000063e-05, 2e-05], + "18:MeanSurfaceVolumetricRateCO2": [ + 1.9999999999987377e-05, + 1.999999999998732e-05, + ], + "18:MeanSurfaceVolumetricRateWater": [ + 1.2681312543855673e-17, + 1.2681312543888312e-17, + ], + } + self.assertEqual( + list(obj.m_wellsPropertiesValues.keys()), + list(expectedPropertiesValues.keys()), + ) + self.assertEqual(obj.m_wellsPropertiesValues, expectedPropertiesValues) + expectedTimesteps: list[float] = [0.0, 100.0] + self.assertEqual(obj.m_timesteps, expectedTimesteps) + expectedDF: pd.DataFrame = pd.DataFrame() + columns_name = [ + "11:Well1Control__BHP__Pa", + "12:Well1Control__TotalMassRate__kg/s", + "13:Well1Control__TotalSurfaceVolumetricRate__m3/s", + "14:Well1Control__SurfaceVolumetricRateCO2__m3/s", + "14:Well1Control__SurfaceVolumetricRateWater__m3/s", + "15:MeanBHP__Pa", + "16:MeanTotalMassRate__kg/s", + "17:MeanTotalVolumetricRate__m3/s", + "18:MeanSurfaceVolumetricRateCO2__m3/s", + "18:MeanSurfaceVolumetricRateWater__m3/s", + "Time__s", + ] + values = [ + [23960094.51907003, 23318529.329811733], + [0.00029566997749602594, 0.00029566997749602507], + [2.0000000000000063e-05, 2e-05], + [1.9999999999987377e-05, 1.999999999998732e-05], + [1.2681312543855673e-17, 1.2681312543888312e-17], + [23960094.51907003, 23318529.329811733], + [0.00029566997749602594, 0.00029566997749602507], + [2.0000000000000063e-05, 2e-05], + [1.9999999999987377e-05, 1.999999999998732e-05], + [1.2681312543855673e-17, 1.2681312543888312e-17], + [0.0, 100.0], + ] + for column_name, value in zip(columns_name, values): + expectedDF[column_name] = value + obtainedDF: pd.DataFrame = obj.createDataframe() + self.assertEqual(list(obtainedDF.columns), columns_name) + self.assertTrue(expectedDF.equals(obtainedDF)) + + def test_invalidWellName(self: Self) -> None: + """Test output message in case of invalid well names.""" + # TODO + # Message being output is not tested in itself :Self, only its appearance + capturedOutput = io.StringIO() + with contextlib.redirect_stdout(capturedOutput): + obj: GeosLogReaderWells = GeosLogReaderWells( + pathFlowSim5, conversionFactors, ["CO2", "water"], 1 + ) + self.assertGreater(len(capturedOutput.getvalue()), 0) + self.assertEqual(obj.m_phaseNames, ["CO2", "water"]) + self.assertEqual(obj.m_wellNames, ["well_1Control"]) + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsInvalidLogs.py b/geos-posp/tests/testsInvalidLogs.py new file mode 100644 index 00000000..dd2bbb57 --- /dev/null +++ b/geos-posp/tests/testsInvalidLogs.py @@ -0,0 +1,66 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Alexandre Benedicto +# ruff: noqa: E402 # disable Module level import not at top of file +import contextlib +import io +import os +import sys +import unittest + +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.readers.GeosLogReaderAquifers import GeosLogReaderAquifers +from geos_posp.readers.GeosLogReaderConvergence import GeosLogReaderConvergence +from geos_posp.readers.GeosLogReaderFlow import GeosLogReaderFlow +from geos_posp.readers.GeosLogReaderWells import GeosLogReaderWells +from geos_posp.utils.UnitRepository import Unit, UnitRepository + +unitsObjSI: UnitRepository = UnitRepository() +conversionFactors: dict[str, Unit] = unitsObjSI.getPropertiesUnit() +pathFlowSim: str = os.path.join(dir_path, "Data/empty.txt") + + +class TestsInvalidLogs(unittest.TestCase): + def test_emptyLog(self: Self) -> None: + """Test empty log.""" + # capturedOutWells = io.StringIO() + with self.assertRaises(AssertionError): + objWells = GeosLogReaderWells( # noqa: F841 + pathFlowSim, conversionFactors, [], 1 + ) + + capturedOutAquif = io.StringIO() + with contextlib.redirect_stdout(capturedOutAquif): + objAquif = GeosLogReaderAquifers( # noqa: F841 + pathFlowSim, conversionFactors + ) + expectedOutAquif: str = ( + "Invalid Geos log file. Please check that your log " + + "did not crash and contains aquifers." + ) + self.assertEqual(capturedOutAquif.getvalue().strip(), expectedOutAquif) + + with self.assertRaises(AssertionError): + objFlow = GeosLogReaderFlow( # noqa: F841 + pathFlowSim, conversionFactors + ) # noqa: F841 + + capturedOutConv = io.StringIO() + with contextlib.redirect_stdout(capturedOutConv): + objConv = GeosLogReaderConvergence( # noqa: F841 + pathFlowSim, conversionFactors + ) + expectedOutConv: str = ( + "Invalid Geos log file. Please check that your log " + "did not crash." + ) + self.assertEqual(capturedOutConv.getvalue().strip(), expectedOutConv) + + +if __name__ == "__main__": + unittest.main() diff --git a/geos-posp/tests/testsMohrCircle.py b/geos-posp/tests/testsMohrCircle.py new file mode 100644 index 00000000..83bda4e9 --- /dev/null +++ b/geos-posp/tests/testsMohrCircle.py @@ -0,0 +1,294 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Martin Lemay +# ruff: noqa: E402 # disable Module level import not at top of file +import os +import sys +import unittest + +import numpy as np +import numpy.typing as npt +from typing_extensions import Self + +dir_path = os.path.dirname(os.path.realpath(__file__)) +parent_dir_path = os.path.join(os.path.dirname(dir_path), "src") +if parent_dir_path not in sys.path: + sys.path.append(parent_dir_path) + +from geos_posp.processing.MohrCircle import MohrCircle +from geos_posp.processing.MohrCoulomb import MohrCoulomb + +circleId = "12453" +stressVector: npt.NDArray[np.float64] = np.array([1.8, 2.5, 5.2, 0.3, 0.4, 0.1]) + +rockCohesion: float = 8.0e8 +frictionAngle: float = 10 * np.pi / 180.0 # in radian + +principalComponentsExpected: tuple[float, float, float] = (1.748, 2.471, 5.281) + + +class TestsMohrCircle(unittest.TestCase): + + def test_MohrCircleInit(self: Self) -> None: + """Test instanciation of MohrCircle objects.""" + mohrCircle: MohrCircle = MohrCircle(circleId) + mohrCircle.setPrincipalComponents(*principalComponentsExpected) + + self.assertSequenceEqual(circleId, mohrCircle.getCircleId()) + + obtained: list[float] = [ + round(val, 3) for val in mohrCircle.getPrincipalComponents() + ] + self.assertSequenceEqual(obtained, principalComponentsExpected) + + def test_MohrCircleRadius(self: Self) -> None: + """Test the calculation of MohrCircle radius.""" + mohrCircle: MohrCircle = MohrCircle(circleId) + mohrCircle.computePrincipalComponents(stressVector) + + obtained: float = mohrCircle.getCircleRadius() + expected: float = ( + principalComponentsExpected[2] - principalComponentsExpected[0] + ) / 2.0 + self.assertAlmostEqual(obtained, expected, 3) + + def test_MohrCircleCenter(self: Self) -> None: + """Test the calculation of MohrCircle center.""" + mohrCircle: MohrCircle = MohrCircle(circleId) + mohrCircle.computePrincipalComponents(stressVector) + + obtained: float = mohrCircle.getCircleCenter() + expected: float = ( + principalComponentsExpected[2] + principalComponentsExpected[0] + ) / 2.0 + self.assertAlmostEqual(obtained, expected, 3) + + +class TestsMohrCoulomb(unittest.TestCase): + + def test_MohrCoulombInit(self: Self) -> None: + """Test instanciation of MohrCoulomb objects.""" + # expected values + expectedSlope: float = np.tan(frictionAngle) + expectedSigmaMin: float = -rockCohesion / expectedSlope + # instantiate object + mohrCoulomb: MohrCoulomb = MohrCoulomb(rockCohesion, frictionAngle) + # test results + self.assertEqual(mohrCoulomb.m_rockCohesion, rockCohesion) + self.assertEqual(mohrCoulomb.m_slope, expectedSlope) + self.assertEqual(mohrCoulomb.m_sigmaMin, expectedSigmaMin) + + def test_computeShearStress(self: Self) -> None: + """Test calculation of shear stress from normal stress.""" + # inputs + stressNormal: npt.NDArray[np.float64] = np.linspace(5.0e8, 1.0e9, 100) + # expected values + expectedValues: npt.NDArray[np.float64] = np.array( + [ + 888163490.0, + 889054031.0, + 889944571.0, + 890835111.0, + 891725652.0, + 892616192.0, + 893506732.0, + 894397273.0, + 895287813.0, + 896178353.0, + 897068893.0, + 897959434.0, + 898849974.0, + 899740514.0, + 900631055.0, + 901521595.0, + 902412135.0, + 903302676.0, + 904193216.0, + 905083756.0, + 905974296.0, + 906864837.0, + 907755377.0, + 908645917.0, + 909536458.0, + 910426998.0, + 911317538.0, + 912208079.0, + 913098619.0, + 913989159.0, + 914879700.0, + 915770240.0, + 916660780.0, + 917551320.0, + 918441861.0, + 919332401.0, + 920222941.0, + 921113482.0, + 922004022.0, + 922894562.0, + 923785103.0, + 924675643.0, + 925566183.0, + 926456724.0, + 927347264.0, + 928237804.0, + 929128344.0, + 930018885.0, + 930909425.0, + 931799965.0, + 932690506.0, + 933581046.0, + 934471586.0, + 935362127.0, + 936252667.0, + 937143207.0, + 938033748.0, + 938924288.0, + 939814828.0, + 940705368.0, + 941595909.0, + 942486449.0, + 943376989.0, + 944267530.0, + 945158070.0, + 946048610.0, + 946939151.0, + 947829691.0, + 948720231.0, + 949610772.0, + 950501312.0, + 951391852.0, + 952282392.0, + 953172933.0, + 954063473.0, + 954954013.0, + 955844554.0, + 956735094.0, + 957625634.0, + 958516175.0, + 959406715.0, + 960297255.0, + 961187795.0, + 962078336.0, + 962968876.0, + 963859416.0, + 964749957.0, + 965640497.0, + 966531037.0, + 967421578.0, + 968312118.0, + 969202658.0, + 970093199.0, + 970983739.0, + 971874279.0, + 972764819.0, + 973655360.0, + 974545900.0, + 975436440.0, + 976326981.0, + ] + ) + # instantiate object + mohrCoulomb: MohrCoulomb = MohrCoulomb(rockCohesion, frictionAngle) + obtained: npt.NDArray[np.float64] = np.array( + mohrCoulomb.computeShearStress(stressNormal) + ) + + # test results + self.assertSequenceEqual(expectedValues.tolist(), np.round(obtained).tolist()) + + def test_computeFailureEnvelop1(self: Self) -> None: + """Test calculation of failure envelop from minimum normal stress.""" + # inputs + stressNormalMax: float = 1.0e9 + # expected values + normalStressExpected: npt.NDArray[np.float64] = np.array( + [ + -4537025456.0, + -3921800405.0, + -3306575354.0, + -2691350304.0, + -2076125253.0, + -1460900203.0, + -845675152.0, + -230450101.0, + 384774949.0, + 1000000000.0, + ] + ) + shearStressExpected: npt.NDArray[np.float64] = np.array( + [ + 0.0, + 108480776.0, + 216961551.0, + 325442327.0, + 433923103.0, + 542403878.0, + 650884654.0, + 759365429.0, + 867846205.0, + 976326981.0, + ] + ) + + # instantiate object + mohrCoulomb: MohrCoulomb = MohrCoulomb(rockCohesion, frictionAngle) + normalStressObtained, shearStressObtained = mohrCoulomb.computeFailureEnvelop( + stressNormalMax, n=10 + ) + + # test results + self.assertSequenceEqual( + normalStressExpected.tolist(), np.round(normalStressObtained).tolist() + ) + self.assertSequenceEqual( + shearStressExpected.tolist(), np.round(shearStressObtained).tolist() + ) + + def test_computeFailureEnvelop2(self: Self) -> None: + """Test calculation of failure envelop in user-defined range.""" + # inputs + stressNormalMin: float = 8.0e8 + stressNormalMax: float = 1.0e9 + # expected values + normalStressExpected: npt.NDArray[np.float64] = np.array( + [ + 800000000.0, + 822222222.0, + 844444444.0, + 866666667.0, + 888888889.0, + 911111111.0, + 933333333.0, + 955555556.0, + 977777778.0, + 1000000000.0, + ] + ) + shearStressExpected: npt.NDArray[np.float64] = np.array( + [ + 941061585.0, + 944979962.0, + 948898339.0, + 952816717.0, + 956735094.0, + 960653471.0, + 964571849.0, + 968490226.0, + 972408603.0, + 976326981.0, + ] + ) + + # instantiate object + mohrCoulomb: MohrCoulomb = MohrCoulomb(rockCohesion, frictionAngle) + normalStressObtained, shearStressObtained = mohrCoulomb.computeFailureEnvelop( + stressNormalMax, stressNormalMin, n=10 + ) + + # test results + self.assertSequenceEqual( + normalStressExpected.tolist(), np.round(normalStressObtained).tolist() + ) + self.assertSequenceEqual( + shearStressExpected.tolist(), np.round(shearStressObtained).tolist() + ) diff --git a/geos-prep/.gitignore b/geos-prep/.gitignore new file mode 100644 index 00000000..bcef4e44 --- /dev/null +++ b/geos-prep/.gitignore @@ -0,0 +1,167 @@ +# Byte-compiled / optimized / DLL files +__pycache__/ +*.py[cod] +*$py.class + +# C extensions +*.so + +# Distribution / packaging +.Python +build/ +develop-eggs/ +dist/ +downloads/ +eggs/ +.eggs/ +lib/ +lib64/ +parts/ +sdist/ +var/ +wheels/ +share/python-wheels/ +*.egg-info/ +.installed.cfg +*.egg +MANIFEST + +# PyInstaller +# Usually these files are written by a python script from a template +# before PyInstaller builds the exe, so as to inject date/other infos into it. +*.manifest +*.spec + +# Installer logs +pip-log.txt +pip-delete-this-directory.txt + +# Unit test / coverage reports +htmlcov/ +.tox/ +.nox/ +.coverage +.coverage.* +.cache +nosetests.xml +coverage.xml +*.cover +*.py,cover +.hypothesis/ +.pytest_cache/ +cover/ + +# Translations +*.mo +*.pot + +# Django stuff: +*.log +local_settings.py +db.sqlite3 +db.sqlite3-journal + +# Flask stuff: +instance/ +.webassets-cache + +# Scrapy stuff: +.scrapy + +# Sphinx documentation +docs/_build/ + +# PyBuilder +.pybuilder/ +target/ + +# Jupyter Notebook +.ipynb_checkpoints + +# IPython +profile_default/ +ipython_config.py + +# pyenv +# For a library or package, you might want to ignore these files since the code is +# intended to run in multiple environments; otherwise, check them in: +.python-version + +# pipenv +# According to pypa/pipenv#598, it is recommended to include Pipfile.lock in version control. +# However, in case of collaboration, if having platform-specific dependencies or dependencies +# having no cross-platform support, pipenv may install dependencies that don't work, or not +# install all needed dependencies. +#Pipfile.lock + +# poetry +# Similar to Pipfile.lock, it is generally recommended to include poetry.lock in version control. +# This is especially recommended for binary packages to ensure reproducibility, and is more +# commonly ignored for libraries. +# https://python-poetry.org/docs/basic-usage/#commit-your-poetrylock-file-to-version-control +#poetry.lock + +# pdm +# Similar to Pipfile.lock, it is generally recommended to include pdm.lock in version control. +#pdm.lock +# pdm stores project-wide configurations in .pdm.toml, but it is recommended to not include it +# in version control. +# https://pdm.fming.dev/latest/usage/project/#working-with-version-control +.pdm.toml +.pdm-python +.pdm-build/ + +# PEP 582; used by e.g. github.com/David-OConnor/pyflow and github.com/pdm-project/pdm +__pypackages__/ + +# Celery stuff +celerybeat-schedule +celerybeat.pid + +# SageMath parsed files +*.sage.py + +# Environments +.env +.venv +env/ +venv/ +ENV/ +env.bak/ +venv.bak/ + +# Spyder project settings +.spyderproject +.spyproject + +# Rope project settings +.ropeproject + +# mkdocs documentation +/site + +# mypy +.mypy_cache/ +.dmypy.json +dmypy.json + +# Pyre type checker +.pyre/ + +# pytype static type analyzer +.pytype/ + +# Cython debug symbols +cython_debug/ + +# PyCharm +# JetBrains specific template is maintained in a separate JetBrains.gitignore that can +# be found at https://github.com/github/gitignore/blob/main/Global/JetBrains.gitignore +# and can be added to the global gitignore or merged into this file. For a more nuclear +# option (not recommended) you can uncomment the following to ignore the entire idea folder. +#.idea/ + +# VScode project +*.vscode/*.json +*.vscode-codespaces* +Thumbs.db diff --git a/geos-prep/README.md b/geos-prep/README.md new file mode 100644 index 00000000..029ba1f5 --- /dev/null +++ b/geos-prep/README.md @@ -0,0 +1,17 @@ +# geos-prep + + +## Description +geos-prep gathers preprocessing tools for [Geos](https://geosx-geosx.readthedocs-hosted.com/en/latest/index.html) hydro-poromechanics simulation software. + +geos-prep is based on [vtk](https://gitlab.kitware.com/vtk/vtk) mesh library and defines [ParaView](https://www.paraview.org/) plugins to use it through an IHM. + +## Installation +The current code has been developed on Python 3.9.13 using the following libraries: + +numpy 1.24.3 +vtk 9.3.2 +paraview 5.11.1 + +> [!CAUTION] +> This package is under construction and needs to be updated with dependencies to common libraries with geos-posp package. \ No newline at end of file diff --git a/geos-prep/pyproject.toml b/geos-prep/pyproject.toml new file mode 100644 index 00000000..6e9c2da7 --- /dev/null +++ b/geos-prep/pyproject.toml @@ -0,0 +1,154 @@ +[build-system] +requires = ["setuptools>=61.2"] +build-backend = "setuptools.build_meta" + +[tool.setuptools] +include-package-data = true + +[tool.setuptools.packages.find] +where = ["src"] +include = ["geos_prep*", "PVplugins*"] +exclude = ['tests*'] + +[project] +name = "geos-prep" +version = "1.0.0" +description = "The Python package geos-prep is dedicated to pre-process data from the geos simulation tool." +authors = [{name = "Martin Lemay", email = "martin.lemay@external.totalenergies.com"}] +license = {text = "Apache-2.0"} +classifiers = [ + "Intended Audience :: Developers", + "Development Status :: 4 - Beta", + "License :: OSI Approved :: Apache Software License ", + "Natural Language :: English", + "Operating System :: OS Independent", + "Programming Language :: Python :: 3 :: Only", + "Topic :: Scientific/Engineering :: Visualization", +] +keywords = [ + "GEOS", + "Simulation", +] +dependencies = [ + "vtk >= 9.3", + "numpy >= 1.26", + "pandas >= 2.2", + "typing_extensions >= 4.12", + "geos_posp >=1.0", +] +requires-python = ">= 3.9" + +[project.optional-dependencies] +dev = ["black", "ruff", "mypy", "sphinx", "sphinx-rtd-theme", "sphinx-autodoc-typehints"] +test = ["coverage", "pytest"] + +[project.readme] +file = "README.md" +content-type = "text/markdown" + +[tool.bumpversion] +current_version = "1.0.0" + +[[tool.bumpversion.files]] +filename = "pyproject.toml" +search = 'version = "{current_version}"' + +[tool.ruff] +target-version = "py39" + +src = ["src"] + +extend-exclude = ["tests/Data", "docs/"] + +# Same as Black. +line-length = 79 +indent-width = 4 + +[tool.ruff.lint] +select = [ + "E", # pycodestyle errors + "W", # pycodestyle warnings + "F", # pyflakes +# "UP", # pyupgrade deactivate since python39 + "B", # flake8-bugbear + "SIM", # flake8-simplify + "ANN", # flake8-annotations + "C4", # flake8-comprehensions + "I", # isort + "D", # pydocstyle +] + +ignore = [ + "E501", # line too long, handled by black + "B008", # do not perform function calls in argument defaults + "C901", # too complex + "W191", # indentation contains tabs + "D100", + "D101", + "D104", # Missing docstring in public package in __init__.py files + "UP007", +] + +# Allow fix for all enabled rules (when `--fix`) is provided. +fixable = ["ALL"] +unfixable = [] + +# Allow unused variables when underscore-prefixed. +dummy-variable-rgx = "^(_+|(_+[a-zA-Z0-9_]*[a-zA-Z0-9]+?))$" + +[tool.ruff.lint.isort] +known-third-party = ["pyvista"] + +#[tool.ruff.lint.pyupgrade] +# Preserve types, even if a file imports `from __future__ import annotations`. +#keep-runtime-typing = true + +[tool.ruff.lint.pydocstyle] +convention = "google" + +[tool.ruff.format] +# Like Black, use double quotes for strings. +quote-style = "double" + +# Like Black, indent with spaces, rather than tabs. +indent-style = "space" + +# Like Black, automatically detect the appropriate line ending. +line-ending = "auto" + +[tool.pytest.ini_options] +addopts = "" +console_output_style = "count" +python_classes = "Test" +python_files = "test*.py" +python_functions = "test*" +testpaths = ["tests"] + +[tool.coverage.run] +branch = true +source = ["PVplugins, geos-prep"] + +[tool.mypy] +# Specify the target platform details in config, so your developers are +# free to run mypy on Windows, Linux, or macOS and get consistent +# results. +python_version = "3.9" +files = "." +exclude = "build/*" +# strict = true + +warn_unreachable = true +implicit_reexport = true +show_error_codes = true +show_column_numbers = true +disable_error_code = "misc" + +# Overrides for currently untyped modules +[[tool.mypy.overrides]] +module = [ + "docs.*", + "docs.ext.*", + "tests.unit.*", +] +ignore_errors = true + diff --git a/geos-trame/.codespellrc b/geos-trame/.codespellrc new file mode 100644 index 00000000..67273fff --- /dev/null +++ b/geos-trame/.codespellrc @@ -0,0 +1,2 @@ +[codespell] +skip =**/package-lock.json,*.vtu diff --git a/geos-trame/.flake8 b/geos-trame/.flake8 new file mode 100644 index 00000000..99b4cf24 --- /dev/null +++ b/geos-trame/.flake8 @@ -0,0 +1,11 @@ +[flake8] + +ignore = + # Black and flake8 conflict here + E203 + # Just assume black did a good job with the line lengths + E501 + W503 + W504 + +exclude = tests/data diff --git a/geos-trame/.gitignore b/geos-trame/.gitignore new file mode 100644 index 00000000..ffdcc545 --- /dev/null +++ b/geos-trame/.gitignore @@ -0,0 +1,29 @@ +.DS_Store +node_modules +.venv + +# local env files +.env.local +.env.*.local + +# Log files +npm-debug.log* +yarn-debug.log* +yarn-error.log* +pnpm-debug.log* + +# Directory which contains screenshot produced by the app +downloaded_files + +# Editor directories and files +.idea +.vscode +*.suo +*.ntvs* +*.njsproj +*.sln +*.sw? + +__pycache__ +*egg-info +*pyc diff --git a/geos-trame/.pre-commit-config.yaml b/geos-trame/.pre-commit-config.yaml new file mode 100644 index 00000000..dc0f9373 --- /dev/null +++ b/geos-trame/.pre-commit-config.yaml @@ -0,0 +1,17 @@ +repos: + - repo: https://github.com/psf/black + rev: 22.3.0 + hooks: + - id: black + exclude: ^.*\b(schema_generated)\b.*$ + entry: black --check --force-exclude + + - repo: https://github.com/codespell-project/codespell + rev: v2.1.0 + hooks: + - id: codespell + + - repo: https://github.com/PyCQA/flake8 + rev: 4.0.1 + hooks: + - id: flake8 diff --git a/geos-trame/CONTRIBUTING.rst b/geos-trame/CONTRIBUTING.rst new file mode 100644 index 00000000..6d5a9c23 --- /dev/null +++ b/geos-trame/CONTRIBUTING.rst @@ -0,0 +1,19 @@ +========================== +Contributing to geos-trame +========================== + +#. Clone the repository using ``git clone`` +#. Install pre-commit via ``pip install pre-commit`` +#. Run ``pre-commit install`` to set up pre-commit hooks +#. Make changes to the code, and commit your changes to a separate branch +#. Create a fork of the repository on GitHub +#. Push your branch to your fork, and open a pull request + +Tips +#### + +#. When first creating a new project, it is helpful to run ``pre-commit run --all-files`` to ensure all files pass the pre-commit checks. +#. A quick way to fix ``black`` issues is by installing black (``pip install black``) and running the ``black`` command at the root of your repository. +#. Sometimes, ``black`` and ``flake8`` do not agree. Add options to your ``.flake8`` file to fix these things. See the `flake8 configuration docs `_ for more details. +#. A quick way to fix ``codespell`` issues is by installing codespell (``pip install codespell``) and running the ``codespell -w`` command at the root of your directory. +#. The `.codespellrc file `_ can be used fix any other codespell issues, such as ignoring certain files, directories, words, or regular expressions. diff --git a/geos-trame/MANIFEST.in b/geos-trame/MANIFEST.in new file mode 100644 index 00000000..819b7aa5 --- /dev/null +++ b/geos-trame/MANIFEST.in @@ -0,0 +1 @@ +graft geos_trame/module/serve diff --git a/geos-trame/README.rst b/geos-trame/README.rst new file mode 100644 index 00000000..797f1948 --- /dev/null +++ b/geos-trame/README.rst @@ -0,0 +1,62 @@ +========== +geos-trame +========== + +GEOS-TRAME is a graphical user interface using Kitware's TRAME technology for GEOS. +It is a client-server dashboard for GEOS users written in python that allows to: + +* visualize GEOS components as a tree structure +* fill the components properties in a dynamically-computed form or as an XML snippet +* visualize the 3D objects (reservoir, fractures, boundary features, wells) on whom simulation will be run +* visualize relative permeability 2D curves dynamically-computed from the simulation deck parameters +* visualize the events of the simulation on an unitless timeline (coarse scale) and in a chart with units (fine scale) + + +Installing +---------- +Build and install the Vue components + +.. code-block:: console + + cd vue-components + npm i + npm run build + cd - + +Install the application + +.. code-block:: console + + pip install -e . + + +Run the application + +.. code-block:: console + + geos-trame -I /path/to/ + +Testing +------- + +To be able to run the test suite, make sure to install the additionals dependencies: + +.. code-block:: python + + pip install -e '.[test]' + +Then you can run the test with `pytest .` + +Regarding GEOS +-------------- + +This application takes an XML file from the GEOS project to load dynamically all of its components. +To be able to do that, we need first to generate the corresponding python class based on a +xsd schema provided by GEOS. + +`For more details `_ + +Features +-------- + +* TODO diff --git a/geos-trame/pyproject.toml b/geos-trame/pyproject.toml new file mode 100644 index 00000000..2b2faa53 --- /dev/null +++ b/geos-trame/pyproject.toml @@ -0,0 +1,131 @@ +[build-system] +requires = ["setuptools>=61.2"] +build-backend = "setuptools.build_meta" + +[project] +name = "geos-trame" +version = "1.0.0" +description = "Geos Simulation Modeler" +authors = [{name = "Lionel Untereiner", email = "lionel.untereiner@external.totalenergies.com"}] +license = {text = "Apache-2.0"} +classifiers = [ + "Development Status :: 4 - Beta", + "Environment :: Web Environment", + "Natural Language :: English", + "Operating System :: OS Independent", + "Programming Language :: Python :: 3 :: Only", + "Programming Language :: JavaScript", + "Topic :: Software Development :: Libraries :: Application Frameworks", + "Topic :: Software Development :: Libraries :: Python Modules", +] +keywords = [ + "Python", + "Interactive", + "Web", + "Application", + "Framework", +] + +dependencies = [ + "typing-extensions==4.12.2", + "trame==3.6.5", + "trame-vuetify==2.7.1", + "trame-code==1.0.1", + "trame-server==3.2.3", + "trame-client==3.5.0", + "trame-simput==2.4.3", + "trame-vtk>=2.8.14", + "matplotlib==3.9.4", + "trame-matplotlib==2.0.3", + "trame-components==2.4.2", + "trame-gantt==0.1.5", + "xsdata==24.5", + "xsdata-pydantic[lxml]==24.5", + "pyvista==0.44.1", + "dpath==2.2.0", + "colorcet==3.1.0", + "funcy==2.0", + "typing_inspect==0.9.0" +] + +[project.optional-dependencies] +build = [ + "build >= 1.2" +] +dev = [ + "pylint", + "mypy", + "black", + "isort" +] +test = [ + "pytest==8.3.3", + "pytest-seleniumbase==4.31.6", + "pixelmatch==0.3.0", + "Pillow==11.0.0", + "pytest-xprocess==1.0.2" +] + +[project.readme] +file = "README.md" +content-type = "text/markdown" + +[project.scripts] +geos-trame = "geos_trame.app.__main__:main" + +[project.entry-points.jupyter_serverproxy_servers] +geos-trame = "geos_trame.app.jupyter:jupyter_proxy_info" + +[tool.setuptools] +license-files = ["LICENSE"] +include-package-data = true + +# [tool.setuptools.packages.find] +# include = ['geos-trame*'] + +[tool.setuptools.package-data] +"*" = ["*.js", "*.css"] + +[tool.pytest.ini_options] +addopts = [ + "--import-mode=importlib", + #addopts = "--cov --cov-report html --cov-report term-missing --cov-fail-under 95" +] +pythonpath = "src/" + +# [tool.coverage.run] +# source = ["src"] + +[tool.bumpversion] +current_version = "1.0.0" + +[[tool.bumpversion.files]] +filename = "pyproject.toml" +search = 'version = "{current_version}"' +replace = 'version = "{new_version}"' + +[tool.pylint] +max-line-length = 88 +disable = [ + "C0103", # (invalid-name) + "C0114", # (missing-module-docstring) + "C0115", # (missing-class-docstring) + "C0116", # (missing-function-docstring) + "R0903", # (too-few-public-methods) + "R0913", # (too-many-arguments) + "W0105", # (pointless-string-statement) +] + +[tool.black] +line-length = 88 +target-version = ['py310'] +include = '\.pyi?$' +extend-exclude = ''' +src/geos_trame/schema_generated/*.py +''' + +[tool.isort] +profile = "black" +src_paths = ["src", "tests"] +blackArgs = ["--preview"] +py_version = 310 \ No newline at end of file diff --git a/geos-trame/src/geos_trame/__init__.py b/geos-trame/src/geos_trame/__init__.py new file mode 100644 index 00000000..4ca94b6a --- /dev/null +++ b/geos-trame/src/geos_trame/__init__.py @@ -0,0 +1,3 @@ +from trame_client.utils.version import get_version + +__version__ = get_version("geos-trame") diff --git a/geos-trame/src/geos_trame/app/__init__.py b/geos-trame/src/geos_trame/app/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-trame/src/geos_trame/app/__main__.py b/geos-trame/src/geos_trame/app/__main__.py new file mode 100644 index 00000000..7fdd3dcd --- /dev/null +++ b/geos-trame/src/geos_trame/app/__main__.py @@ -0,0 +1,35 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from pathlib import Path + +from trame.app import get_server + +from geos_trame.app.core import GeosTrame + + +def main(server=None, **kwargs): + # Get or create server + if server is None: + server = get_server() + + if isinstance(server, str): + server = get_server(server) + + # Set client type + server.client_type = "vue3" + + # parse args + parser = server.cli + parser.add_argument("-I", "--input", help="Input file (.xml)") + + (args, _unknown) = parser.parse_known_args() + + if args.input is None: + print("Usage: \n\tgeos-trame -I /path/to/input/file") + return + + file_name = str(Path(args.input).absolute()) + + app = GeosTrame(server, file_name) + app.server.start(**kwargs) diff --git a/geos-trame/src/geos_trame/app/core.py b/geos-trame/src/geos_trame/app/core.py new file mode 100644 index 00000000..af123bde --- /dev/null +++ b/geos-trame/src/geos_trame/app/core.py @@ -0,0 +1,189 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from trame.ui.vuetify3 import VAppLayout +from trame.decorators import TrameApp +from trame.widgets import html, simput +from trame.widgets import vuetify3 as vuetify +from trame_simput import get_simput_manager + +from geos_trame import module +from geos_trame.app.deck.tree import DeckTree +from geos_trame.app.ui.editor import DeckEditor +from geos_trame.app.ui.inspector import DeckInspector +from geos_trame.app.ui.plotting import DeckPlotting +from geos_trame.app.ui.timeline import TimelineEditor +from geos_trame.app.ui.viewer import DeckViewer + +import sys + + +@TrameApp() +class GeosTrame: + def __init__(self, server, file_name: str): + + self.server = server + server.enable_module(module) + + self.state.input_file = file_name + + # TODO handle hot_reload + + # Set state variables of the App + self.state.trame__title = "geos-trame" + self.state.simput_loaded = False + + # Simput configuration + self.simput_manager = get_simput_manager() + self.state.sm_id = self.simput_manager.id + self.simput_widget = simput.Simput( + self.simput_manager, prefix="geos", trame_server=server + ) + self.simput_widget.auto_update = True + + # Controller + self.ctrl.simput_apply = self.simput_widget.apply + self.ctrl.simput_reset = self.simput_widget.reset + self.ctrl.simput_reload_data = self.simput_widget.reload_data + + # Tree + self.tree = DeckTree(self.state.sm_id) + + # TODO put as a modal window + self.set_input_file(file_name=self.state.input_file) + + # Load components + self.ui = self.build_ui() + + @property + def state(self): + return self.server.state + + @property + def ctrl(self): + return self.server.controller + + def set_input_file(self, file_name, file_str=None): + """sets the input file of the InputTree object and populates simput/ui""" + self.tree.set_input_file(file_name) + + def deck_ui(self): + """Generates the UI for the deck edition / visualization tab""" + with vuetify.VRow(classes="mb-6 fill-height"): + with vuetify.VCol( + cols=2, + order=1, + ): + self.deckInspector = DeckInspector( + source=self.tree, classes="fill-height" + ) + + with vuetify.VCol( + cols=10, + order=2, + ): + self.timelineEditor = TimelineEditor( + source=self.tree, classes="ma-2", style="height: 40%" + ) + with vuetify.VRow( + classes="mb-6 fill-height", + ): + + with vuetify.VCol( + cols=5, + order=3, + ): + self.deckEditor = DeckEditor( + source=self.tree, + classes="ma-2", + style="flex: 1; height: 100%;", + ) + + with vuetify.VCol( + cols=7, + order=4, + ): + self.deckViewer = DeckViewer( + source=self.tree, + classes="ma-2", + style="flex: 1; height: 60%; width: 100%;", + ) + + self.deckPlotting = DeckPlotting( + source=self.tree, + classes="ma-2", + style="flex: 1; height: 40%; width: 100%;", + ) + + def build_ui(self, *args, **kwargs): + """Generates the full UI for the GEOS Trame Application""" + + with VAppLayout(self.server) as layout: + self.simput_widget.register_layout(layout) + + def on_tab_change(tab_idx): + pass + + with html.Div( + style="position: relative; display: flex; border-bottom: 1px solid gray", + ): + with vuetify.VTabs( + v_model=("tab_idx", 0), + style="z-index: 1;", + color="grey", + change=(on_tab_change, "[$event]"), + ): + for tab_label in ["Input File", "Execute", "Results Viewer"]: + vuetify.VTab(tab_label) + + with html.Div( + style="position: absolute; top: 0; left: 0; height: 100%; width: 100%; display: flex; align-items: center; justify-content: center;", + ): + with html.Div( + v_if=("tab_idx == 0",), + style="height: 100%; width: 100%; display: flex; align-items: center; justify-content: flex-end;", + ): + with vuetify.VBtn( + click=self.tree.write_files, + icon=True, + style="z-index: 1;", + id="save-button", + ): + vuetify.VIcon("mdi-content-save-outline") + + with html.Div( + style="height: 100%; width: 300px; display: flex; align-items: center; justify-content: space-between;", + v_if=("tab_idx == 1",), + ): + vuetify.VBtn( + "Run", + # click=self.executor.run, + # disabled=( + # "exe_running || exe_use_threading && exe_threads < 2 || exe_use_mpi && exe_processes < 2", + # ), + style="z-index: 1;", + ) + vuetify.VBtn( + "Kill", + # click=self.executor.kill, + # disabled=("!exe_running",), + style="z-index: 1;", + ) + vuetify.VBtn( + "Clear", + # click=self.ctrl.terminal_clear, + style="z-index: 1;", + ) + + # input file editor + with vuetify.VCol( + v_show=("tab_idx == 0",), classes="flex-grow-1 pa-0 ma-0" + ): + if self.tree.input_file is not None: + self.deck_ui() + else: + + print( + "Cannot build ui as the input file cannot be parse.", + file=sys.stderr, + ) diff --git a/geos-trame/src/geos_trame/app/deck/file.py b/geos-trame/src/geos_trame/app/deck/file.py new file mode 100644 index 00000000..1ef0907e --- /dev/null +++ b/geos-trame/src/geos_trame/app/deck/file.py @@ -0,0 +1,458 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +import os +import re +import typing +from dataclasses import fields, is_dataclass +from io import StringIO +from typing import Any, Iterator, List, TextIO + +import typing_extensions +import typing_inspect +from lxml import etree as ElementTree # type: ignore[import-untyped] +from pydantic import BaseModel + +# from xsdata.formats.dataclass.context import XmlContext +# from xsdata.formats.dataclass.parsers import XmlParser +from xsdata.formats.dataclass.parsers.config import ParserConfig + +# from xsdata.formats.dataclass.serializers import DictEncoder +# from xsdata.formats.dataclass.serializers import XmlSerializer +from xsdata.formats.dataclass.serializers.config import SerializerConfig +from xsdata.utils import text +from xsdata_pydantic.bindings import DictEncoder, XmlContext, XmlParser, XmlSerializer + +# from geos_trame.app.deck.inspector import object_to_tree +from geos_trame.app.geosTrameException import GeosTrameException +from geos_trame.schema_generated.schema_mod import Problem + +from geos_trame.app.io.xml_parser import XMLParser + + +def get_origin(v: typing.Any) -> typing.Any: + pydantic_generic_metadata = getattr( + v, "__pydantic_generic_metadata__", None + ) #: PydanticGenericMetadata | None + if pydantic_generic_metadata: + return pydantic_generic_metadata.get("origin") + return typing_extensions.get_origin(v) + + +def all_fields(c: type, already_checked) -> list[str]: + resolved_hints = typing.get_type_hints(c) + field_names = [field.name for field in fields(c)] + resolved_field_types = {name: resolved_hints[name] for name in field_names} + + field_list = [] + for key in resolved_field_types: + current_type = resolved_field_types[key] + if typing_inspect.get_origin(current_type) in (list, typing.List): + inner_type = typing_inspect.get_args(current_type)[0] + if inner_type not in already_checked: + already_checked.append(inner_type) + field_list.extend(all_fields(inner_type, already_checked)) + if is_dataclass(current_type) and current_type not in already_checked: + already_checked.append(current_type) + field_list.extend(all_fields(current_type, already_checked)) + + # {"id": i, "name": f, "children": [], "hidden_children": []} + + return field_list + + +def required_fields(model: type[BaseModel], recursive: bool = False) -> Iterator[str]: + for name, field in model.model_fields.items(): + print(name) + if not field.is_required(): + continue + t = field.annotation + print(t) + if recursive and isinstance(t, type) and issubclass(t, BaseModel): + yield from required_fields(t, recursive=True) + else: + yield name + + +def is_pydantic_model(obj): + try: + return issubclass(obj, BaseModel) + except TypeError: + return False + + +def show_hierarchy(Model: BaseModel, processed_types: set, indent: int = 0): + print(type(Model).__name__) + if type(Model).__name__ not in processed_types: + processed_types.add(type(Model).__name__) + print(processed_types) + for k, v in Model.model_fields.items(): + print( + f'{" "*indent}{k}: ' + f"type={v.annotation}, " + f"required={v.is_required()}" + ) + if is_pydantic_model(typing.get_args(v.annotation)[0]): + # print("plop") + show_hierarchy( + typing.get_args(v.annotation)[0], processed_types, indent + 2 + ) + + +def normalize_path(x): + tmp = os.path.expanduser(x) + tmp = os.path.abspath(tmp) + if os.path.isfile(tmp): + x = tmp + return x + + +class DeckFile(object): + """ + Holds the information of a deck file. + Can be empty. + """ + + def __init__(self, filename: str, **kwargs) -> None: + """ + Constructor. + Input: + filename: file name of the deck file + """ + super(DeckFile, self).__init__(**kwargs) + + self.root_node = None + self.filename = normalize_path(filename) + if self.filename: + self.open_deck_file(self.filename) + self.original_text = "" + self.changed = False + + self.path = os.path.dirname(self.filename) + + def open_deck_file(self, filename: str) -> None: + """ + Opens a file and parses it. + Input: + filename: file name of the input file + Signals: + input_file_changed: On success + Raises: + GeosTrameException: On invalid input file + """ + + self.changed = False + self.root_node = None + + # Do some basic checks on the filename to make sure + # it is probably a real input file since the GetPot + # parser doesn't do any checks. + if not os.path.exists(filename): + msg = "Input file %s does not exist" % filename + raise GeosTrameException(msg) + + if not os.path.isfile(filename): + msg = "Input file %s is not a file" % filename + raise GeosTrameException(msg) + + if not filename.endswith(".xml"): + msg = "Input file %s does not have the proper extension" % filename + raise GeosTrameException(msg) + + self.xml_parser = XMLParser(filename=filename) + self.xml_parser.build() + simulation_deck = self.xml_parser.get_simulation_deck() + + context = XmlContext( + element_name_generator=text.pascal_case, + attribute_name_generator=text.camel_case, + ) + parser = XmlParser( + context=context, config=ParserConfig() + ) # fail_on_unknown_properties=True, fail_on_unknown_attributes=True, fail_on_converter_warnings=True)) + try: + self.problem = parser.parse(simulation_deck, Problem) + except ElementTree.XMLSyntaxError as e: + msg = "Failed to parse input file %s:\n%s\n" % (filename, e) + raise GeosTrameException(msg) + + encoder = DictEncoder(context=context, config=SerializerConfig(indent=" ")) + self.pb_dict = {"Problem": encoder.encode(self.problem)} + self.inspect_tree = build_inspect_tree(encoder.encode(self.problem)) + + def to_str(self) -> str: + config = SerializerConfig(indent=" ", xml_declaration=False) + context = XmlContext( + element_name_generator=text.pascal_case, + attribute_name_generator=text.camel_case, + ) + serializer = XmlSerializer(context=context, config=config) + return serializer.render(self.problem) + + +def build_inspect_tree(obj, *, dict_factory=dict) -> dict: + """Return the fields of a dataclass instance as a new dictionary mapping + field names to field values. + + Example usage:: + + @dataclass + class C: + x: int + y: int + + c = C(1, 2) + assert asdict(c) == {'x': 1, 'y': 2} + + If given, 'dict_factory' will be used instead of built-in dict. + The function applies recursively to field values that are + dataclass instances. This will also look into built-in containers: + tuples, lists, and dicts. Other objects are copied with 'copy.deepcopy()'. + """ + # if not _is_dataclass_instance(obj): + # raise TypeError("asdict() should be called on dataclass instances") + + return _build_inspect_tree_inner("Problem", obj, []) + + +def _build_inspect_tree_inner(key, obj, path) -> dict: + sub_node = dict() + if "name" in obj: + sub_node["title"] = obj["name"] + else: + sub_node["title"] = key + # sub_node["id"] = randrange(150) + sub_node["children"] = list() + # sub_node["hidden_children"] = list() + sub_node["is_drawable"] = key in [ + "VTKMesh", + "InternalMesh", + "InternalWell", + "Perforation", + ] + sub_node["drawn"] = False + + for key, value in obj.items(): + + if isinstance(value, list): + for idx, item in enumerate(value): + if isinstance(item, dict): + more_results = _build_inspect_tree_inner( + key, item, path + [key] + [idx] + ) + # for another_result in more_results: + sub_node["children"].append(more_results) + + # sub_node["path"] = path + [sub_node["name"]] + sub_node["id"] = "Problem/" + "/".join(map(str, path)) + + return sub_node + + +def format_attribute(attribute_indent: str, ka: str, attribute_value: str) -> str: + """Format xml attribute strings + + Args: + attribute_indent (str): Attribute indent string + ka (str): Attribute name + attribute_value (str): Attribute value + + Returns: + str: Formatted attribute value + """ + # Make sure that a space follows commas + attribute_value = re.sub(r",\s*", ", ", attribute_value) + + # Handle external brackets + attribute_value = re.sub(r"{\s*", "{ ", attribute_value) + attribute_value = re.sub(r"\s*}", " }", attribute_value) + + # Consolidate whitespace + attribute_value = re.sub(r"\s+", " ", attribute_value) + + # Identify and split multi-line attributes + if re.match(r"\s*{\s*({[-+.,0-9a-zA-Z\s]*},?\s*)*\s*}", attribute_value): + split_positions: List[Any] = [ + match.end() for match in re.finditer(r"}\s*,", attribute_value) + ] + newline_indent = "\n%s" % (" " * (len(attribute_indent) + len(ka) + 4)) + new_values = [] + for a, b in zip([None] + split_positions, split_positions + [None]): + new_values.append(attribute_value[a:b].strip()) + if new_values: + attribute_value = newline_indent.join(new_values) + + return attribute_value + + +def format_xml_level( + output: TextIO, + node: ElementTree.Element, + level: int, + indent: str = " " * 2, + block_separation_max_depth: int = 2, + modify_attribute_indent: bool = False, + sort_attributes: bool = False, + close_tag_newline: bool = False, + include_namespace: bool = False, +) -> None: + """Iteratively format the xml file + + Args: + output (file): the output text file handle + node (lxml.etree.Element): the current xml element + level (int): the xml depth + indent (str): the xml indent style + block_separation_max_depth (int): the maximum depth to separate adjacent elements + modify_attribute_indent (bool): option to have flexible attribute indentation + sort_attributes (bool): option to sort attributes alphabetically + close_tag_newline (bool): option to place close tag on a separate line + include_namespace (bool): option to include the xml namespace in the output + """ + + # Handle comments + if node.tag is ElementTree.Comment: + output.write("\n%s" % (indent * level, node.text)) + + else: + # Write opening line + opening_line = "\n%s<%s" % (indent * level, node.tag) + output.write(opening_line) + + # Write attributes + if len(node.attrib) > 0: + # Choose indentation + attribute_indent = "%s" % (indent * (level + 1)) + if modify_attribute_indent: + attribute_indent = " " * (len(opening_line)) + + # Get a copy of the attributes + attribute_dict = {} + attribute_dict = node.attrib + + # Sort attribute names + akeys = list(attribute_dict.keys()) + if sort_attributes: + akeys = sorted(akeys) + + # Format attributes + for ka in akeys: + # Avoid formatting mathpresso expressions + if not ( + node.tag in ["SymbolicFunction", "CompositeFunction"] + and ka == "expression" + ): + attribute_dict[ka] = format_attribute( + attribute_indent, ka, attribute_dict[ka] + ) + + for ii in range(0, len(akeys)): + k = akeys[ii] + if (ii == 0) & modify_attribute_indent: + # TODO: attrib_ute_dict isn't define here which leads to an error + # output.write(' %s="%s"' % (k, attrib_ute_dict[k])) + pass + else: + output.write( + '\n%s%s="%s"' % (attribute_indent, k, attribute_dict[k]) + ) + + # Write children + if len(node): + output.write(">") + Nc = len(node) + for ii, child in zip(range(Nc), node): + format_xml_level( + output, + child, + level + 1, + indent, + block_separation_max_depth, + modify_attribute_indent, + sort_attributes, + close_tag_newline, + include_namespace, + ) + + # Add space between blocks + if ( + (level < block_separation_max_depth) + & (ii < Nc - 1) + & (child.tag is not ElementTree.Comment) + ): + output.write("\n") + + # Write the end tag + output.write("\n%s" % (indent * level, node.tag)) + else: + if close_tag_newline: + output.write("\n%s/>" % (indent * level)) + else: + output.write("/>") + + +def format_xml( + input: str, + indent_size: int = 2, + indent_style: bool = False, + block_separation_max_depth: int = 2, + alphebitize_attributes: bool = False, + close_style: bool = False, + namespace: bool = False, +) -> None: + """Script to format xml files + + Args: + input (str): Input str + indent_size (int): Indent size + indent_style (bool): Style of indentation (0=fixed, 1=hanging) + block_separation_max_depth (int): Max depth to separate xml blocks + alphebitize_attributes (bool): Alphebitize attributes + close_style (bool): Style of close tag (0=same line, 1=new line) + namespace (bool): Insert this namespace in the xml description + """ + try: + root = ElementTree.fromstring(input) + # root = tree.getroot() + prologue_comments = [tmp.text for tmp in root.itersiblings(preceding=True)] + epilog_comments = [tmp.text for tmp in root.itersiblings()] + + f = StringIO() + f.write('\n') + + for comment in reversed(prologue_comments): + f.write("\n" % (comment)) + + format_xml_level( + f, + root, + 0, + indent=" " * indent_size, + block_separation_max_depth=block_separation_max_depth, + modify_attribute_indent=indent_style, + sort_attributes=alphebitize_attributes, + close_tag_newline=close_style, + include_namespace=namespace, + ) + + for comment in epilog_comments: + f.write("\n" % (comment)) + f.write("\n") + + return f.getvalue() + + except ElementTree.ParseError as err: + print("\nCould not load file: %s" % (f)) + print(err.msg) + raise Exception("\nCheck input file!") + + +if __name__ == "__main__": + import sys + + if len(sys.argv) < 2: + print("Need an input file as argument") + exit(1) + filename = sys.argv[1] + deck_file = DeckFile(filename) + print(deck_file.root_fields) diff --git a/geos-trame/src/geos_trame/app/deck/tree.py b/geos-trame/src/geos_trame/app/deck/tree.py new file mode 100644 index 00000000..5d16a4bd --- /dev/null +++ b/geos-trame/src/geos_trame/app/deck/tree.py @@ -0,0 +1,408 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +import dpath +import funcy + +import os + +from xsdata.formats.dataclass.parsers.config import ParserConfig +from xsdata.formats.dataclass.serializers.config import SerializerConfig +from xsdata.utils import text +from xsdata_pydantic.bindings import DictDecoder, XmlContext, XmlSerializer + +from geos_trame.app.geosTrameException import GeosTrameException +from geos_trame.schema_generated.schema_mod import BaseModel, Problem, Included, File + +from .file import DeckFile, format_xml, normalize_path + +from collections import defaultdict +from trame_simput import get_simput_manager + + +def recursive_dict(element): + return element.tag, dict(map(recursive_dict, element)) or element.text + + +class DeckTree(object): + """ + A tree that represents an deck file along with all the available blocks and parameters. + """ + + def __init__(self, sm_id=None, **kwds): + """ + Constructor. + """ + super(DeckTree, self).__init__(**kwds) + + self.input_file = None + self.input_filename = None + self.input_folder = None + self.input_real_filename = None + # self._copyDefaultTree() + self.root = None + self.path_map = {} + self.input_has_errors = False + self._sm_id = sm_id + + def set_input_file(self, input_filename): + """ + Set a new input file + Input: + input_filename[str]: The name of the input file + Return: + bool: If it was a valid input file + """ + try: + self.input_filename = input_filename + self.input_file = DeckFile(self.input_filename) + self.input_folder = os.path.dirname(self.input_file.filename) + self.input_real_filename = os.path.basename(self.input_file.filename) + except Exception as e: + msg = "set_input_file exception: %s" % e + return GeosTrameException(msg) + + def root_fields(self) -> list[str]: + return self.input_file.root_fields + + def get_mesh(self) -> str: + return normalize_path( + self.input_file.path + "/" + self.input_file.problem.mesh[0].vtkmesh[0].file + ) + + def get_abs_path(self, file) -> str: + return normalize_path(self.input_file.path + "/" + file) + + def to_str(self) -> str: + return self.input_file.to_str() + + def get_tree(self) -> dict: + return self.input_file.inspect_tree + + def update(self, path, key, value) -> None: + new_path = [int(x) if x.isdigit() else x for x in path.split("/")] + new_path.append(key) + funcy.set_in(self.input_file.pb_dict, new_path, value) + + def search(self, path) -> dict: + new_path = [int(x) if x.isdigit() else x for x in path.split("/")] + if self.input_file is None: + return + return dpath.values(self.input_file.pb_dict, new_path) + + def decode(self, path): + data = self.search(path) + if data is None: + return + + context = XmlContext( + element_name_generator=text.pascal_case, + attribute_name_generator=text.camel_case, + ) + decoder = DictDecoder(context=context, config=ParserConfig()) + node = decoder.decode(data[0]) + return node + + def decode_data(self, data: BaseModel) -> str: + """ + Convert a data to a xml serializable file + """ + if data is None: + return + + context = XmlContext( + element_name_generator=text.pascal_case, + attribute_name_generator=text.camel_case, + ) + decoder = DictDecoder(context=context, config=ParserConfig()) + node = decoder.decode(data) + return node + + def to_xml(self, obj) -> str: + context = XmlContext( + element_name_generator=text.pascal_case, + attribute_name_generator=text.camel_case, + ) + + config = SerializerConfig(indent=" ", xml_declaration=False) + serializer = XmlSerializer(context=context, config=config) + + return format_xml(serializer.render(obj)) + + def timeline(self) -> dict: + if self.input_file is None: + return + if self.input_file.problem is None: + return + if self.input_file.problem.events is None: + return + + timeline = list() + # list root events + global_id = 0 + for e in self.input_file.problem.events[0].periodic_event: + item = dict() + item["id"] = global_id + item["summary"] = e.name + item["start_date"] = e.begin_time + timeline.append(item) + global_id = global_id + 1 + + return timeline + + def plots(self): + return self.input_file.problem.functions + + def write_files(self): + """ + Write geos files with all changes made by the user. + """ + + pb = self.search("Problem") + files = self._split(pb) + + for filepath, content in files.items(): + includeName: str = self.input_file.xml_parser.file_to_relative_path[ + filepath + ] + model_loaded: BaseModel = self.decode_data(content) + model_with_changes: BaseModel = self._apply_changed_properties(model_loaded) + self._append_include_file(model_with_changes, includeName) + + model_as_xml: str = self.to_xml(model_with_changes) + + basename = os.path.basename(filepath) + edited_folder_path = self.input_folder + location = edited_folder_path + "/" + self._append_id(basename) + with open(location, "w") as file: + file.write(model_as_xml) + file.close() + + def _setInputFile(self, input_file): + """ + Copies the nodes of an input file into the tree + Input: + input_file[InputFile]: Input file to copy + Return: + bool: True if successful + """ + self.input_has_errors = False + if input_file.root_node is None: + return False + self.input_file = input_file + self.input_filename = input_file.filename + + return False + + def _append_include_file(self, model: Problem, includedFilePath: str) -> None: + """ + Append an Included object which follows this structure according to the documentation: + + + + + Only Problem can contains an included tag: + https://geosx-geosx.readthedocs-hosted.com/en/latest/docs/sphinx/datastructure/CompleteXMLSchema.html + + """ + if len(includedFilePath) == 0: + return None + + includedTag = Included() + includedTag.file.append(File(name=self._append_id(includedFilePath))) + + model.included.append(includedTag) + + def _append_id(self, filename: str) -> str: + """ + Return the new filename with the correct suffix and his extension. The suffix + added will be '_vX' where X is the incremented value of the current version. + '_v0' if any suffix is present. + """ + name, ext = os.path.splitext(filename) + name_length = len(name) + + suffix = "_v" + version = 0 + suffix_pos = name_length - 3 + if name_length > 3 and name.endswith(suffix, suffix_pos, name_length - 1): + version_str = name[name_length - 1 :] + version = int(version_str) + 1 + name = name[: name_length - 3] + + suffix += str(version) + return f"{name}{suffix}{ext}" + + def _convert_to_camel_case(self, content: str) -> str: + """ + Convert any given string in CamelCase. + + Useful to transform trame_simput convention in geos schema names convention. + """ + camel_case_str: str = content.title() + return camel_case_str.replace("_", "") + + def _convert_to_snake_case(self, content: str) -> str: + """ + Convert any given string in snake case. + + Useful to transform geos schema names convention in trame_simput convention. + """ + return "".join( + ["_" + char.lower() if char.isupper() else char for char in content] + ).lstrip("_") + + def _apply_changed_properties(self, model: Problem) -> Problem: + """ + Retrieves all edited 'properties' from the simput_manager and apply it to a + given model. + + """ + + manager = get_simput_manager(self._sm_id) + modified_proxy_ids: set[str] = manager.proxymanager.dirty_proxy_data + + if len(modified_proxy_ids) == 0: + return model + + model_as_dict = dict(model) + + for proxy_id in modified_proxy_ids: + properties = manager.data(proxy_id)["properties"] + events = self._get_base_model_from_path(model_as_dict, proxy_id) + if events is None: + continue + events_as_dict = dict(events) + for property_name, value in properties.items(): + events_as_dict[property_name] = value + + self._set_base_model_properties(model_as_dict, proxy_id, events_as_dict) + + model = getattr(model, "model_validate")(model_as_dict) + return model + + def _convert_proxy_path_into_proxy_names(self, proxy_path: str) -> list[str]: + """ + Split a given proxy path into a list of proxy names. + + note: each proxy name will be converted in snake case to fit with the + pydantic model naming convention. + """ + splitted_path = proxy_path.split("/") + splitted_path_without_root = splitted_path[1:] + + return [ + self._convert_to_snake_case(proxy) for proxy in splitted_path_without_root + ] + + def _set_base_model_properties( + self, model: dict, proxy_path: str, properties: dict + ) -> None: + """ + Apply all changed property to the model for a specific proxy. + """ + + # retrieve the whole BaseModel list to the modified proxy + proxy_names = self._convert_proxy_path_into_proxy_names(proxy_path) + model_copy = model + models = [] + for proxy_name in proxy_names: + is_dict = type(model_copy) is dict + is_list = type(model_copy) is list + is_class = not is_dict and not is_list + + if is_class: + model_copy = dict(model_copy) + + if proxy_name.isnumeric() and int(proxy_name) < len(model_copy): + models.append([proxy_name, model_copy]) + model_copy = model_copy[int(proxy_name)] + continue + + if proxy_name in model_copy: + models.append([proxy_name, model_copy]) + model_copy = model_copy[proxy_name] + else: + return None + + models.reverse() + + # propagate the modification to the parent node + index = -1 + for model_inverted in models: + prop_identifier = model_inverted[0] + + if prop_identifier.isnumeric(): + index = int(prop_identifier) + continue + + if index == -1: + continue + + current_node = model_inverted[1] + current_base_model = current_node[prop_identifier][index] + current_base_model = getattr(current_base_model, "model_validate")( + properties + ) + + current_node[prop_identifier][index] = current_base_model + + properties = dict(current_base_model) + break + + models.reverse() + model = models[0] + + def _get_base_model_from_path(self, model: dict, proxy_id: str) -> BaseModel: + """ + Retrieve the BaseModel changed from the proxy id. The proxy_id is a unique path + from the simput manager. + """ + proxy_names = self._convert_proxy_path_into_proxy_names(proxy_id) + + model_found: dict = model + + for proxy_name in proxy_names: + + is_dict = type(model_found) is dict + is_list = type(model_found) is list + is_class = not is_dict and not is_list + + if is_class: + model_found = dict(model_found) + + # path can contains a numerical index, useful to be sure that each + # proxy is unique, typically used for a list of proxy located at the same level + if proxy_name.isnumeric() and int(proxy_name) < len(model_found): + model_found = model_found[int(proxy_name)] + continue + + if proxy_name in model_found: + model_found = model_found[proxy_name] + + return model_found + + def _split(self, xml: str) -> dict[str, str]: + data = self.input_file.xml_parser.file_to_tags + restructured_files = defaultdict(dict) + for file_path, associated_tags in data.items(): + restructured_files[file_path] = dict() + for tag, contents in xml[0].items(): + if len(contents) == 0: + continue + tag_formatted = tag + if tag_formatted in associated_tags: + restructured_files[file_path][tag] = contents + + return restructured_files + + +if __name__ == "__main__": + import sys + + if len(sys.argv) < 3: + print("Usage: ") + exit(1) + input_file_path = sys.argv[2] + deck_tree = DeckTree() + deck_tree.setInputFile(input_file_path) diff --git a/geos-trame/src/geos_trame/app/geosTrameException.py b/geos-trame/src/geos_trame/app/geosTrameException.py new file mode 100644 index 00000000..4fe900cd --- /dev/null +++ b/geos-trame/src/geos_trame/app/geosTrameException.py @@ -0,0 +1,13 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +class GeosTrameException(Exception): + pass + + +class FileExistsException(GeosTrameException): + pass + + +class BadExecutableException(GeosTrameException): + pass diff --git a/geos-trame/src/geos_trame/app/io/__init__.py b/geos-trame/src/geos_trame/app/io/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-trame/src/geos_trame/app/io/xml_parser.py b/geos-trame/src/geos_trame/app/io/xml_parser.py new file mode 100644 index 00000000..ce369580 --- /dev/null +++ b/geos-trame/src/geos_trame/app/io/xml_parser.py @@ -0,0 +1,212 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +import os +import re +from os.path import expandvars +from pathlib import Path + +from lxml import etree as ElementTree +from lxml.etree import XMLSyntaxError + +from collections import defaultdict + +from geos_trame.app.geosTrameException import GeosTrameException + + +class XMLParser(object): + """ + Class used to parse a valid XML geos file and construct a link between + each file when they are included. + + Useful to be able to able to save it later. + """ + + def __init__(self, filename: str) -> None: + """ + Constructor which takes in input the xml file used to generate pedantic file. + """ + + self.filename = filename + self.file_to_tags = defaultdict(list) + self.file_to_relative_path = {} + + expanded_file = Path(expandvars(self.filename)).expanduser().resolve() + self.file_path = expanded_file.parent + self._is_valid = True + + try: + parser = ElementTree.XMLParser(remove_comments=True, remove_blank_text=True) + tree = ElementTree.parse(expanded_file, parser=parser) + self.root = tree.getroot() + except XMLSyntaxError as err: + error_msg = "Invalid XML file. Cannot load " + expanded_file + error_msg += ". Outputted error:\n" + err.msg + print(error_msg, file=os.sys.stderr) + self._is_valid = False + + def is_valid(self) -> bool: + if not self._is_valid: + print("XMLParser isn't valid", file=os.sys.stderr) + return self._is_valid + + def build(self) -> None: + if not self.is_valid(): + raise GeosTrameException("Cannot parse this file.") + self._read() + + def get_simulation_deck(self) -> ElementTree.Element: + if not self.is_valid(): + raise GeosTrameException("Not valid file, cannot return the deck.") + return + return self.simulation_deck + + def _read(self) -> ElementTree.Element: + """Reads an xml file (and recursively its included files) into memory + + Args: + xmlFilepath (str): The path the file to read. + + Returns: + SimulationDeck: The simulation deck + """ + for include_node in self.root: + tags = self.file_to_tags[self.filename] + tags.append(include_node.tag) + + includeCount = 0 + for include_node in self.root: + if include_node.tag == "Included": + for f in include_node.findall("File"): + self.file_to_relative_path[self.filename] = f.get("name") + self._merge_included_xml_files( + self.root, self.file_path, f.get("name"), includeCount + ) + + # Remove 'Included' nodes + for include_node in self.root.findall("Included"): + self.root.remove(include_node) + + for neighbor in self.root.iter(): + for key in neighbor.attrib.keys(): + # remove unnecessary whitespaces for indentation + s = re.sub(r"\s{2,}", " ", neighbor.get(key)) + neighbor.set(key, s) + + self.simulation_deck = self.root + + def _merge_xml_nodes( + self, + existingNode: ElementTree.Element, + targetNode: ElementTree.Element, + fname: str, + level: int, + ) -> None: + """Merge nodes in an included file into the current structure level by level. + + Args: + existingNode (lxml.etree.Element): The current node in the base xml structure. + targetNode (lxml.etree.Element): The node to insert. + level (int): The xml file depth. + """ + if not self.is_valid(): + raise GeosTrameException("Not valid file, cannot merge nodes") + return + # Copy attributes on the current level + for tk in targetNode.attrib.keys(): + existingNode.set(tk, targetNode.get(tk)) + + # Copy target children into the xml structure + currentTag = "" + matchingSubNodes = [] + + for target in targetNode.getchildren(): + tags = self.file_to_tags[fname] + tags.append(target.tag) + insertCurrentLevel = True + + # Check to see if a node with the appropriate type + # exists at this level + if currentTag != target.tag: + currentTag = target.tag + matchingSubNodes = existingNode.findall(target.tag) + + if matchingSubNodes: + targetName = target.get("name") + + # Special case for the root Problem node (which may be unnamed) + if level == 0: + insertCurrentLevel = False + self._merge_xml_nodes(matchingSubNodes[0], target, fname, level + 1) + + # Handle named xml nodes + elif targetName and (currentTag not in ["Nodeset"]): + for match in matchingSubNodes: + if match.get("name") == targetName: + insertCurrentLevel = False + self._merge_xml_nodes(match, target, fname, level + 1) + + # Insert any unnamed nodes or named nodes that aren't present + # in the current xml structure + if insertCurrentLevel: + existingNode.insert(-1, target) + + def _merge_included_xml_files( + self, + root: ElementTree.Element, + file_path: str, + fname: str, + includeCount: int, + maxInclude: int = 100, + ) -> None: + """Recursively merge included files into the current structure. + + Args: + root (lxml.etree.Element): The root node of the base xml structure. + fname (str): The name of the target xml file to merge. + includeCount (int): The current recursion depth. + maxInclude (int): The maximum number of xml files to include (default = 100) + """ + if not self.is_valid(): + raise GeosTrameException("Not valid file, cannot merge nodes") + return + included_file_path = Path(expandvars(file_path), fname) + expanded_file = included_file_path.expanduser().resolve() + + self.file_to_relative_path[fname] = "" + + # Check to see if the code has fallen into a loop + includeCount += 1 + if includeCount > maxInclude: + raise Exception( + "Reached maximum recursive includes... Is there an include loop?" + ) + + # Check to make sure the file exists + if not included_file_path.is_file(): + print( + "Included file does not exist: %s" % (included_file_path), + file=os.sys.stderr, + ) + raise Exception("Check included file path!") + + # Load target xml + try: + parser = ElementTree.XMLParser(remove_comments=True, remove_blank_text=True) + includeTree = ElementTree.parse(included_file_path, parser) + includeRoot = includeTree.getroot() + except XMLSyntaxError as err: + print("\nCould not load included file: %s" % (included_file_path)) + print(err.msg) + raise Exception("\nCheck included file!") from err + + # Recursively add the includes: + for include_node in includeRoot.findall("Included"): + for f in include_node.findall("File"): + self.file_to_relative_path[fname] = f.get("name") + self._merge_included_xml_files( + root, expanded_file.parent, f.get("name"), includeCount + ) + + # Merge the results into the xml tree + self._merge_xml_nodes(root, includeRoot, fname, 0) diff --git a/geos-trame/src/geos_trame/app/ui/editor.py b/geos-trame/src/geos_trame/app/ui/editor.py new file mode 100644 index 00000000..63524ca6 --- /dev/null +++ b/geos-trame/src/geos_trame/app/ui/editor.py @@ -0,0 +1,98 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from trame.widgets import code, simput +from trame.widgets import vuetify3 as vuetify +from trame_simput import get_simput_manager + + +class DeckEditor(vuetify.VCard): + def __init__(self, source=None, **kwargs): + super().__init__(**kwargs) + + self.tree = source + self.simput_manager = get_simput_manager(id=self.state.sm_id) + + self.state.active_ids = [] + self.state.active_id = "Problem" + self.state.active_name = "Problem" + + self.state.active_snippet = "" + self.state.change("active_id")(self.on_active_id) + + with self: + with vuetify.VCardTitle("Components editor"): + vuetify.VTextField( + v_model=("active_name"), + v_if=("active_name != null",), + label="Name", + dense=True, + hide_details=True, + ) + vuetify.VSpacer() + vuetify.VTextField( + v_model=("active_type"), + v_if=("active_type != null",), + readonly=True, + label="Type", + dense=True, + hide_details=True, + ) + vuetify.VSpacer() + vuetify.VSwitch(v_model=("code", False), label="view XML snippet") + vuetify.VDivider() + + with vuetify.VCardText( + v_if="!code", + ): + simput.SimputItem( + item_id=("active_id", None), + ) + + code.Editor( + v_if="code", + style="height: 100vh", + value=("active_snippet", ""), + options=( + "editor_options", + { + "automaticLayout": True, + "scrollbar": {"vertical": True, "horizontal": True}, + "layoutInfo": {"width": 80}, + }, + ), + language=("editor_lang", "xml"), + theme=("editor_theme", "vs-dark"), + textmate=("editor_textmate", None), + ) + + def on_active_id(self, active_id, **kwargs): + # this function triggers when a block is selected from the tree in the ui + + if active_id is None: + self.state.active_name = "Mesh" + self.state.active_type = None + self.state.active_types = [] + return + + active_block = self.tree.decode(active_id) + + simput_type = type(active_block).__name__ + + self.simput_manager.proxymanager.get_instances_of_type(simput_type) + + self.state.active_id = active_id + self.state.active_ids = [active_id] + + if hasattr(active_block, "name"): + self.state.active_name = active_block.name + else: + self.state.active_name = None + + if active_block is None: + return + + self.state.active_type = simput_type + self.state.active_types = [simput_type] + + self.state.active_snippet = self.tree.to_xml(active_block) diff --git a/geos-trame/src/geos_trame/app/ui/inspector.py b/geos-trame/src/geos_trame/app/ui/inspector.py new file mode 100644 index 00000000..a145e6aa --- /dev/null +++ b/geos-trame/src/geos_trame/app/ui/inspector.py @@ -0,0 +1,309 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from dataclasses import dataclass +from enum import StrEnum + +import yaml +from pydantic import BaseModel +from trame.widgets import vuetify3 as vuetify +from trame_simput import get_simput_manager +from typing import Any + + +class Renderable(StrEnum): + VTKMESH = "VTKMesh" + INTERNALMESH = "InternalMesh" + INTERNALWELL = "InternalWell" + PERFORATION = "Perforation" + + +# Pure pydantic version +# +# class TreeNode(BaseModel): +# id: str +# name: str +# is_drawable: bool +# drawn: bool +# children: list['TreeNode'] +# hidden_children: list['TreeNode'] + +# def get_node(obj, node_id, path): +# children = [] +# for name, info in obj.model_fields.items(): +# if name in obj.model_fields_set: +# print(type(info)) +# print(name, "-", info.annotation, " - ", get_origin(info.annotation), get_args(info.annotation)[0]) +# metadata = getattr(info, "xsdata_metadata", None) or {} +# print(metadata["name"]) +# if get_origin(info.annotation) is list: +# attr= getattr(obj, name) +# print(attr) +# for idx, item in enumerate(attr): +# children.append(get_node(item, name, path + [name] + [idx])) + +# return TreeNode( +# id = "Problem/" + "/".join(map(str, path)), +# name = "metadata", +# children = children, +# hidden_children = [], +# is_drawable = node_id in Renderable, +# drawn = False, +# ) + + +@dataclass +class TreeNode: + id: str + title: str + children: list + hidden_children: list + is_drawable: bool + drawn: bool + + @property + def json(self) -> dict: + if self.children: + return dict( + id=self.id, + title=self.title, + is_drawable=self.is_drawable, + drawn=self.drawn, + children=[c.json for c in self.children], + hidden_children=[c.json for c in self.hidden_children], + ) + return dict( + id=self.id, + title=self.title, + is_drawable=self.is_drawable, + drawn=self.drawn, + children=None, + hidden_children=[], + ) + + +def get_node_dict(obj, node_id, path): + children = [] + for key, value in obj.items(): + # todo look isinstance(value, dict): + if isinstance(value, list): + for idx, item in enumerate(value): + if isinstance(item, dict): + children.append(get_node_dict(item, key, path + [key] + [idx])) + + node_name = node_id + if "name" in obj: + node_name = obj["name"] + + return TreeNode( + id="Problem/" + "/".join(map(str, path)), + title=node_name, + children=children if len(children) else [], + hidden_children=[], + is_drawable=node_id in (k for k in Renderable), + drawn=False, + ) + + +def object_to_tree(obj: dict) -> dict: + return get_node_dict(obj, "Problem", []).json + + +def dump(item): + match item: + case BaseModel() as model: + subitems: dict[str, Any] = dict() + model.model_fields + + for field, value in model: + + if isinstance(value, str): + subitems[field] = value + continue + + return subitems + case list() | tuple() | set(): # pyright: ignore + # Pyright finds this disgusting; this passes `mypy` though. ` # type: + # ignore` would fail `mypy` is it'd be unused (because there's nothing to + # ignore because `mypy` is content) + # return type(container)( # pyright: ignore + # _dump(i) for i in container # pyright: ignore + # ) + pass + case dict(): + # return { + # k: _dump(v) + # for k, v in item.items() # pyright: ignore[reportUnknownVariableType] + # } + pass + case _: + return item + + +def iterate_nested_dict(iterable, returned="key"): + """Returns an iterator that returns all keys or values + of a (nested) iterable. + + Arguments: + - iterable: or + - returned: "key" or "value" + + Returns: + - + """ + + if isinstance(iterable, dict): + for key, value in iterable.items(): + if key == "id": + if not (isinstance(value, dict) or isinstance(value, list)): + yield value + # else: + # raise ValueError("'returned' keyword only accepts 'key' or 'value'.") + for ret in iterate_nested_dict(value, returned=returned): + yield ret + elif isinstance(iterable, list): + for el in iterable: + for ret in iterate_nested_dict(el, returned=returned): + yield ret + + +vuetify.enable_lab() + + +class DeckInspector(vuetify.VTreeview): + def __init__(self, listen_to_active=True, source=None, **kwargs): + super().__init__( + # data + items=("deck_tree",), + item_value="id", + **{ + # style + "hoverable": True, + "rounded": True, + # "dense": True, + # "density": "compact", + # "active_color": "blue", + # activation logic + # "activatable": True, + # "active_strategy": "single-independent", + # "activated": ("active_ids", ), + # "update_activated": "(active_ids) => {active_id = active_ids[0]}", + # selection logic + "selectable": True, + "select_strategy": "single-independent", + "selected": ("active_ids",), + "update_selected": "(active_ids) => {active_id = active_ids[0]}", + **kwargs, + }, + ) + self.tree = source + self._source = None + self.listen_to_active = listen_to_active + + self.state.obj_path = "" + + # register used types from Problem + self.simput_types = [] + + self.simput_manager = get_simput_manager(id=self.state.sm_id) + + if source.input_file is None: + return + + self.set_source(source.input_file.problem) + + def on_change(topic, ids=None, **kwargs): + if topic == "changed": + for obj_id in ids: + proxy = self.simput_manager.proxymanager.get(obj_id) + self.tree.decode(obj_id) + for prop in proxy.edited_property_names: + self.tree.update(obj_id, prop, proxy.get_property(prop)) + + self.simput_manager.proxymanager.on(on_change) + + with self: + with vuetify.Template(v_slot_append="{ item }"): + with vuetify.VBtn( + v_if=("item.is_drawable"), + icon=True, + flat=True, + slim=True, + input_value=("item.drawn"), + click=(self.to_draw_change, "[item.id]"), + ): + vuetify.VIcon( + "{{ ((item.drawn)) ? 'mdi-eye' : 'mdi-eye-off' }}", + v_if=("item.is_drawable"), + ) + + @property + def source(self): + return self._source + + # TODO + # v should be a proxy like the one in paraview simple + # maybe it can be Any of schema_mod (e.g. Problem) + def set_source(self, v): + + # TODO replace this snippet + from xsdata.formats.dataclass.serializers.config import SerializerConfig + from xsdata.utils import text + from xsdata_pydantic.bindings import DictEncoder, XmlContext + + context = XmlContext( + element_name_generator=text.pascal_case, + attribute_name_generator=text.camel_case, + ) + + encoder = DictEncoder(context=context, config=SerializerConfig(indent=" ")) + self._source = encoder.encode(v) + # with this one by passing v as Problem + # self._source = v + + if v is None: + self.state.deck_tree = [] + else: + self.state.deck_tree = object_to_tree(self._source).get("children", []) + + for v in iterate_nested_dict(self.state.deck_tree): + + active_block = self.tree.decode(v) + # active_name = None + + # if hasattr(active_block, "name"): + # active_name = active_block.name + + simput_type = type(active_block).__name__ + + test = dump(active_block) + + if test: + params_dict = {} + for key, value in test.items(): + params_dict[key] = { + # "initial": str(v), + "type": "string", + } + + self.simput_types.append(simput_type) + yaml_str = yaml.dump({simput_type: params_dict}, sort_keys=False) + + self.simput_manager.load_model(yaml_content=yaml_str) + + debug = self.simput_manager.proxymanager.create(simput_type, proxy_id=v) + + for key, value in test.items(): + debug.set_property(key, getattr(active_block, key)) + debug.commit() + + def to_draw_change(self, path): + self.state.obj_path = path + + # def on_active_change(self, **_): + # if self.listen_to_active: + # print("on_active_change") + # self.set_source_proxy(simple.GetActiveSource()) + + # def on_selection_change(self, node_active, **_): + # print("on_selection_change", node_active) diff --git a/geos-trame/src/geos_trame/app/ui/plotting.py b/geos-trame/src/geos_trame/app/ui/plotting.py new file mode 100644 index 00000000..547a1865 --- /dev/null +++ b/geos-trame/src/geos_trame/app/ui/plotting.py @@ -0,0 +1,98 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +import matplotlib.pyplot as plt +import numpy as np +from trame.widgets import matplotlib +from trame.widgets import vuetify3 as vuetify + + +class DeckPlotting(vuetify.VCard): + def __init__(self, source=None, **kwargs): + super().__init__(**kwargs) + + self._source = source + if source.input_file is None: + return + + self._filepath = (source.input_file.path,) + + self.ctrl.permeability = self.permeability + self.ctrl.figure_size = self.figure_size + + with self: + vuetify.VCardTitle("2D View") + html_viewX = matplotlib.Figure( + figure=self.ctrl.permeability(**self.ctrl.figure_size()), + # style="position: absolute;left: 20%;top: 30%;", + ) + self.ctrl.update_figure = html_viewX.update + + @property + def source(self): + return self._source + + def update_view(self, **kwargs): + self.ctrl.view_update(figure=self.ctrl.permeability(**self.ctrl.figure_size())) + + def figure_size(self): + + if self.state.figure_size is None: + return {} + + dpi = self.state.figure_size.get("dpi") + rect = self.state.figure_size.get("size") + w_inch = rect.get("width") / dpi / 2 + h_inch = rect.get("height") / dpi / 2 + + return { + "figsize": (w_inch, h_inch), + "dpi": dpi, + } + + def inverse_gaz(self, x): + return 1 - x + + def permeability(self, **kwargs): + # read data + for f in self.source.plots(): + for t in f.table_function: + if t.name == "waterRelativePermeabilityTable": + fileX = t.coordinate_files.strip("{(.+)}").strip() + self.water_x = np.loadtxt(self.source.input_file.path + "/" + fileX) + self.water_y = np.loadtxt( + self.source.input_file.path + "/" + t.voxel_file + ) + + if t.name == "gasRelativePermeabilityTable": + fileX = t.coordinate_files.strip("{(.+)}").strip() + + gaz_x = np.loadtxt(self.source.input_file.path + "/" + fileX) + self.gaz_x = self.inverse_gaz(gaz_x) + self.gaz_y = np.loadtxt( + self.source.input_file.path + "/" + t.voxel_file + ) + + # make drawing + plt.close("all") + fig, ax = plt.subplots(**kwargs) + + if ( + self.water_x is not None + and self.water_y is not None + and self.gaz_x is not None + and self.gaz_y is not None + ): + np.random.seed(0) + ax.plot(self.water_x, self.water_y, label="water") + ax.plot(self.gaz_x, self.gaz_y, label="gaz") + + ax.set_xlabel("Water saturation") + ax.set_ylabel("Relative permeability") + ax.set_title("Matplotlib Plot Rendered in D3!", size=14) + ax.grid(color="lightgray", alpha=0.7) + plt.xlim([0, 1]) + plt.ylim([0, 1]) + plt.legend() + + return fig diff --git a/geos-trame/src/geos_trame/app/ui/timeline.py b/geos-trame/src/geos_trame/app/ui/timeline.py new file mode 100644 index 00000000..7f87585c --- /dev/null +++ b/geos-trame/src/geos_trame/app/ui/timeline.py @@ -0,0 +1,121 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from trame.widgets import code, gantt, html, simput +from trame.widgets import vuetify3 as vuetify +from trame_simput import get_simput_manager + + +class TimelineEditor(vuetify.VCard): + def __init__(self, source=None, **kwargs): + super().__init__(**kwargs) + + self.tree = source + self.simput_manager = get_simput_manager(id=self.state.sm_id) + + items = self.tree.timeline() + # print(items) + + # DRAFT + # items = [ + # {"id": 1, + # "summary": "outputInjectionPeriod", + # "start_date": "2024-11-02 00:00", + # "end_date": "2024-11-02 00:00", + # "duration": 23 + # }, + # { + # "id": 2, + # "summary": "This is a task with a longer description.", + # "start_date": "2024-11-03 00:00", + # "end_date": "2024-11-04 00:00", + # "duration": 1 + # } + # ] + + items_alt = [ + { + "id": 3, + "summary": "Lorem ipsum.", + "start_date": "2024-11-07 00:00", + "end_date": "2024-11-09 00:00", + "duration": 2, + } + ] + + fields = [ + { + "summary": { + "label": "Summary", + "component": "gantt-text", + "width": 300, + "placeholder": "Add a new task...", + }, + "start_date": { + "label": "Start", + "component": "gantt-date", + "width": 75, + "placeholder": "Start", + "sort": "date", + }, + "end_date": { + "label": "End", + "component": "gantt-date", + "width": 75, + "placeholder": "End", + "sort": "date", + }, + "duration": { + "label": "Days", + "component": "gantt-number", + "width": 50, + "placeholder": "0", + }, + } + ] + + with self: + # with vuetify.VRow( + # rows=2, + # style="width: 100%;", + # dense=True + # classes="fill-height" + # ): + vuetify.VCardTitle("Events View") + vuetify.VDateInput( + label="Select starting simulation date", + prepend_icon="", + prepend_inner_icon="$calendar", + placeholder="09/18/2024", + ) + vuetify.VDivider() + with vuetify.VContainer("Events timeline"): + with vuetify.VTimeline( + direction="horizontal", + truncate_line="both", + align="center", + side="end", + ): # , truncate_line="both", side="end", line_inset="12"): + with vuetify.VTimelineItem( + v_for=(f"item in {items}",), key="i", value="item", size="small" + ): + vuetify.VAlert("{{ item.summary }}") + vuetify.Template( + "{{ item.start_date }}", raw_attrs=["v-slot:opposite"] + ) + + with vuetify.VContainer("Events chart"): + gantt.Gantt( + canEdit=True, + dateLimit=30, + startDate="2024-11-01 00:00", + endDate="2024-12-01 00:00", + # title='Gantt-pre-test', + fields=fields, + update=(self.update_from_js, "items"), + items=("items", items), + classes="fill_height", + ) + + def update_from_js(self, *items): + self.state.items = list(items) diff --git a/geos-trame/src/geos_trame/app/ui/viewer.py b/geos-trame/src/geos_trame/app/ui/viewer.py new file mode 100644 index 00000000..7dbd03ae --- /dev/null +++ b/geos-trame/src/geos_trame/app/ui/viewer.py @@ -0,0 +1,302 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +import pyvista as pv +from pyvista.trame.ui import plotter_ui +from trame.widgets import html, vtk +from trame.widgets import vuetify3 as vuetify + +from geos_trame.schema_generated.schema_mod import InternalWell, Vtkmesh + +# def setup_viewer(): +# pl = pv.Plotter() + +# p.reset_camera() + +# return p.ren_vin + +# prevents launching an external window with rendering +pv.OFF_SCREEN = True + + +class RegionViewer: + def __init__(self) -> None: + self.input: pv.UnstructuredGrid = pv.UnstructuredGrid() + self.mesh: pv.UnstructuredGrid + + def __call__(self, normal: tuple[float], origin: tuple[float]) -> None: + self.update_clip(normal, origin) + + def add_mesh(self, mesh: pv.UnstructuredGrid) -> None: + self.input = mesh # type: ignore + self.mesh = self.input.copy() # type: ignore + + def update_clip(self, normal: tuple[float], origin: tuple[float]) -> None: + self.mesh.copy_from(self.input.clip(normal=normal, origin=origin, crinkle=True)) # type: ignore + + +# class WellViewer: +# def __init__(self, size: float, amplification: float) -> None: +# self.input: list[pv.PolyData] = [] +# self.tubes: list[pv.PolyData] = [] +# self.size: float = size +# self.amplification: float = amplification +# self.STARTING_VALUE: float = 5.0 + +# def __call__(self, value: float) -> None: +# self.update(value) + +# def add_mesh(self, mesh: pv.PolyData) -> None: +# self.input.append(mesh) # type: ignore +# radius = self.size * (self.STARTING_VALUE / 100) +# self.tubes.append( +# mesh.tube( +# radius=radius, n_sides=50 +# ) # .scale([1.0, 1.0, self.amplification], inplace=True) +# ) # type: ignore + +# def update(self, value: float) -> None: +# radius = self.size * (value / 100) +# for idx, m in enumerate(self.input): +# self.tubes[idx].copy_from( +# m.tube( +# radius=radius, n_sides=50 +# ) # .scale([1.0, 1.0, self.amplification], inplace=True) +# ) + + +# class GeosPlotterBase: +# def add_region(self, mesh: pv.UnstructuredGrid, name: str, zscale: int = 1) -> None: +# super().add_mesh(mesh, name=name, **kwargs) + +# def add_well(self, mesh: pv.PolyData, name: str, zscale: int = 1) -> None: +# # build tube +# super().add_mesh() + +# def update_clip(self, normal: tuple[float], origin: tuple[float]) -> None: +# pass +# # for m in super().meshes: +# # m. + + +# class GeosPlotter(GeosPlotterBase, pv.Plotter): +# pass + + +### VIEWER + + +def button(click, icon, tooltip): # numpydoc ignore=PR01 + """Create a vuetify button.""" + with vuetify.VTooltip(bottom=True): + with vuetify.Template(v_slot_activator="{ on, attrs }"): + with vuetify.VBtn(icon=True, v_bind="attrs", v_on="on", click=click): + vuetify.VIcon(icon) + html.Span(tooltip) + + +def checkbox(model, icons, tooltip): # numpydoc ignore=PR01 + """Create a vuetify checkbox.""" + with vuetify.VTooltip(bottom=True): + with vuetify.Template(v_slot_activator="{ on, attrs }"): + with html.Div(v_on="on", v_bind="attrs"): + vuetify.VCheckbox( + v_model=model, + on_icon=icons[0], + off_icon=icons[1], + dense=True, + hide_details=True, + classes="my-0 py-0 ml-1", + ) + html.Span(tooltip) + + +def spin_edit(model, tooltip): # numpydoc ignore=PR01 + """Create a vuetify slider.""" + with vuetify.VTooltip(bottom=True): + with vuetify.Template(v_slot_activator="{ on, attrs }"): + with html.Div(v_on="on", v_bind="attrs"): + vuetify.VTextField( + v_model=model, + dense=True, + hide_details=True, + classes="my-0 py-0 ml-1", + type="number", + counter="3", + # counter_value= + ) + html.Span(tooltip) + + +class DeckViewer(vuetify.VCard): + def __init__(self, source, **kwargs): + super().__init__(**kwargs) + + self._source = source + self._pl = pv.Plotter() + + self.CUT_PLANE = f"_cut_plane_visibility" + self.ZAMPLIFICATION = f"_z_amplification" + self.server.state[self.CUT_PLANE] = False + self.server.state[self.ZAMPLIFICATION] = 1 + + self.state.change("obj_path")(self.add_to_3dviewer) + + self.region_engine = RegionViewer() + + # self.well_engine = WellViewer() + + with self: + vuetify.VCardTitle("3D View") + view = plotter_ui( + self._pl, + add_menu_items=self.rendering_menu_extra_items, + style="position: absolute;", + ) + self.ctrl.view_update = view.update + + @property + def plotter(self): + return self._pl + + @property + def source(self): + return self._source + + def rendering_menu_extra_items(self): + self.state.change(self.CUT_PLANE)(self.on_cut_plane_visiblity_change) + vuetify.VDivider(vertical=True, classes="mr-3") + # html.Span('foo', classes="mr-3") + # spin_edit( + # model=(self.ZAMPLIFICATION, 3), + # tooltip=f"Z Amplification", + # ) + + # tooltip=f"Toggle cut plane visibility ({{{{ {self.CUT_PLANE} ? 'on' : 'off' }}}})", + # with vuetify.VBtn( + # icon=True, + # # v_on="on", + # # v_bind="attrs", + # # click="(event) => {event.stopPropagation(); event.preventDefault();}", + # ): + # vuetify.VIcon( + # "mdi-plus-circle", + # ) + + def on_cut_plane_visiblity_change(self, **kwargs): + pass + """Toggle cut plane visibility for all actors. + + Parameters + ---------- + **kwargs : dict, optional + Unused keyword arguments. + + """ + # value = kwargs[self.CUT_PLANE] + # for renderer in self.plotter.renderers: + # for actor in renderer.actors.values(): + # if isinstance(actor, pyvista.Actor): + # actor.prop.show_edges = value + # self.update() + + def add_to_3dviewer(self, obj_path, **kwargs): + path = obj_path + + if path == "": + return + + active_block = self.source.decode(path) + + # def update_tree(entry, search_id): + + # print("entry :", entry) + # print("search_id : ", search_id) + + # print(entry["id"]) + # if entry["id"] == search_id: + # entry["drawn"] = True + # return + + # for child in entry["children"]: + # update_tree(child, search_id) + # for child in entry["hidden_children"]: + # update_tree(child, search_id) + + # print(self.server.state.deck_tree[0]) + # update_tree(self.server.state.deck_tree, path) + # self.server.state.dirty("deck_tree") + + if isinstance(active_block, Vtkmesh): + self.region_engine.add_mesh( + pv.read(self.source.get_abs_path(active_block.file)) + ) + self.plotter.add_mesh_clip_plane( + self.region_engine.mesh, + origin=self.region_engine.mesh.center, + normal=[-1, 0, 0], + crinkle=True, + show_edges=False, + cmap="glasbey_bw", + # cmap=cmap, + # clim=clim, + # categories=True, + scalars="attribute", + # n_colors=n, + ) + + self.server.controller.view_update() + + if isinstance(active_block, InternalWell): + s = active_block.polyline_node_coords + points = np.array(literal_eval(s.translate(tr)), dtype=np.float64) + tip = points[0] + + s = active_block.polyline_segment_conn + lines = np.array(literal_eval(s.translate(tr)), dtype=np.int64) + v_indices = np.unique(lines.flatten()) + + r = literal_eval(active_block.radius.translate(tr)) + radius = np.repeat(r, points.shape[0]) + + vpoints = vtk.vtkPoints() + vpoints.SetNumberOfPoints(points.shape[0]) + vpoints.SetData(numpy_to_vtk(points)) + + polyLine = vtk.vtkPolyLine() + polyLine.GetPointIds().SetNumberOfIds(len(v_indices)) + + for iline, vidx in enumerate(v_indices): + polyLine.GetPointIds().SetId(iline, vidx) + + cells = vtk.vtkCellArray() + cells.InsertNextCell(polyLine) + + vradius = vtk.vtkDoubleArray() + vradius.SetName("radius") + vradius.SetNumberOfComponents(1) + vradius.SetNumberOfTuples(points.shape[0]) + vradius.SetVoidArray(numpy_to_vtk(radius), points.shape[0], 1) + + polyData = vtk.vtkPolyData() + polyData.SetPoints(vpoints) + polyData.SetLines(cells) + polyData.GetPointData().AddArray(vradius) + polyData.GetPointData().SetActiveScalars("radius") + + bounds = self.region_engine.mesh.bounds + + xsize = bounds[1] - bounds[0] + ysize = bounds[3] - bounds[2] + + maxsize = max(xsize, ysize) + self.well_engine = WellViewer(maxsize, 1) + + self.well_engine.add_mesh(pv.wrap(polyData)) + + for m in self.well_engine.tubes: + actor = self.plotter.add_mesh(m, color=True, show_edges=False) + + self.server.controller.view_update() + + # if isinstance(active_block, Perforation): diff --git a/geos-trame/src/geos_trame/module/.gitignore b/geos-trame/src/geos_trame/module/.gitignore new file mode 100644 index 00000000..f1066395 --- /dev/null +++ b/geos-trame/src/geos_trame/module/.gitignore @@ -0,0 +1,5 @@ +# serve +serve/*.map +serve/*.html +serve/*.common.* +serve/*.umd.js \ No newline at end of file diff --git a/geos-trame/src/geos_trame/module/__init__.py b/geos-trame/src/geos_trame/module/__init__.py new file mode 100644 index 00000000..f772bedc --- /dev/null +++ b/geos-trame/src/geos_trame/module/__init__.py @@ -0,0 +1,25 @@ +from pathlib import Path + +# Compute local path to serve +serve_path = str(Path(__file__).with_name("serve").resolve()) + +# Serve directory for JS/CSS files +serve = {"__geos_trame": serve_path} + +# List of JS files to load (usually from the serve path above) +scripts = ["__geos_trame/geos_trame.umd.js"] + +# List of CSS files to load (usually from the serve path above) +# styles = ["__geos_trame/style.css"] + +# List of Vue plugins to install/load +vue_use = ["geos_trame"] + +# Uncomment to add entries to the shared state +# state = {} + + +# Optional if you want to execute custom initialization at module load +def setup(app, **kwargs): + """Method called at initialization with possibly some custom keyword arguments""" + pass diff --git a/geos-trame/src/geos_trame/schema_generated/README.md b/geos-trame/src/geos_trame/schema_generated/README.md new file mode 100644 index 00000000..cca98585 --- /dev/null +++ b/geos-trame/src/geos_trame/schema_generated/README.md @@ -0,0 +1,59 @@ +# Schema Generation + +This folder contains auto-generated file based on an xsd file from the GEOS repository. + +We should not modify manually these files. + +## Context + +Input files from GEOS are described as an xml which follow a specific schema. To be able +to parse, serialize and deserialize these files in trame with `trame-simput`, we need to +generate a serializable class for each balise described in the schema used by GEOS. + +For that we use a python module named `xsd-pydantic` which allows us to generate a file. +It will contain all class for a given xsd schema file. + +When starting the trame application, we can instantiate the expected dataclass when parsing +the input file. + +## How to generate a new file + +#### 1. Clone the GEOS Repository + +```bash +git clone git@github.com:GEOS-DEV/GEOS.git +``` + +#### 2. Create a dedicate venv + +```bash +cd +python -m venv pydantic-venv +source pydantic-venv/bin/activate +pip install -e . +pip install "xsdata[cli]" +cd src/geos_trame/schema_generated +``` + +#### 3. Generate the new file + +The full documentation is [here](https://xsdata-pydantic.readthedocs.io/en/latest/codegen/). + +```bash +xsdata /src/coreComponents/schema/schema.xsd --output pydantic --package generated_models --structure-style single-package --include-header +``` + +Then update the generated file, at the beginning, by adding the geos commit used: + +For example: + +```py +"""This file was generated by xsdata, v24.6.1, on 2024-11-29 + +Generator: PydanticGenerator +See: https://xsdata.readthedocs.io/ + +GEOS commit hash: +""" +``` + diff --git a/geos-trame/src/geos_trame/schema_generated/old_schema_mod.py b/geos-trame/src/geos_trame/schema_generated/old_schema_mod.py new file mode 100644 index 00000000..146844f3 --- /dev/null +++ b/geos-trame/src/geos_trame/schema_generated/old_schema_mod.py @@ -0,0 +1,16565 @@ +"""This file was generated by xsdata, v24.4, on 2024-04-23 11:59:25 + +Generator: PydanticGenerator +See: https://xsdata.readthedocs.io/ +""" + +from __future__ import annotations + +from dataclasses import field +from typing import List, Optional + +from pydantic.dataclasses import dataclass + + +@dataclass(kw_only=True) +class Aquifer: + class Meta: + name = "AquiferType" + + allow_all_phases_into_aquifer: str = field( + default="0", + metadata={ + "name": "allowAllPhasesIntoAquifer", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + aquifer_angle: str = field( + metadata={ + "name": "aquiferAngle", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_elevation: str = field( + metadata={ + "name": "aquiferElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_initial_pressure: str = field( + metadata={ + "name": "aquiferInitialPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_inner_radius: str = field( + metadata={ + "name": "aquiferInnerRadius", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_permeability: str = field( + metadata={ + "name": "aquiferPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_porosity: str = field( + metadata={ + "name": "aquiferPorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_thickness: str = field( + metadata={ + "name": "aquiferThickness", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_total_compressibility: str = field( + metadata={ + "name": "aquiferTotalCompressibility", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_water_density: str = field( + metadata={ + "name": "aquiferWaterDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_water_phase_component_fraction: str = field( + default="{0}", + metadata={ + "name": "aquiferWaterPhaseComponentFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + aquifer_water_phase_component_names: str = field( + default="{}", + metadata={ + "name": "aquiferWaterPhaseComponentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + aquifer_water_viscosity: str = field( + metadata={ + "name": "aquiferWaterViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + pressure_influence_function_name: Optional[str] = field( + default=None, + metadata={ + "name": "pressureInfluenceFunctionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class BiotPorosity: + class Meta: + name = "BiotPorosityType" + + default_porosity_tec: str = field( + default="0", + metadata={ + "name": "defaultPorosityTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_reference_porosity: str = field( + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + grain_bulk_modulus: str = field( + metadata={ + "name": "grainBulkModulus", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + use_uniaxial_fixed_stress: str = field( + default="0", + metadata={ + "name": "useUniaxialFixedStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class BlackOilFluid: + class Meta: + name = "BlackOilFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hydrocarbon_formation_vol_factor_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonFormationVolFactorTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + hydrocarbon_viscosity_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonViscosityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + surface_densities: str = field( + metadata={ + "name": "surfaceDensities", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + table_files: str = field( + default="{}", + metadata={ + "name": "tableFiles", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + water_compressibility: str = field( + default="0", + metadata={ + "name": "waterCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_formation_volume_factor: str = field( + default="0", + metadata={ + "name": "waterFormationVolumeFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_reference_pressure: str = field( + default="0", + metadata={ + "name": "waterReferencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_viscosity: str = field( + default="0", + metadata={ + "name": "waterViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Blueprint: + class Meta: + name = "BlueprintType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_full_quadrature_data: str = field( + default="0", + metadata={ + "name": "outputFullQuadratureData", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Box: + class Meta: + name = "BoxType" + + strike: str = field( + default="-90", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + x_max: str = field( + metadata={ + "name": "xMax", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + x_min: str = field( + metadata={ + "name": "xMin", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class BrooksCoreyBakerRelativePermeability: + class Meta: + name = "BrooksCoreyBakerRelativePermeabilityType" + + gas_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "gasOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "waterOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class BrooksCoreyCapillaryPressure: + class Meta: + name = "BrooksCoreyCapillaryPressureType" + + cap_pressure_epsilon: str = field( + default="1e-06", + metadata={ + "name": "capPressureEpsilon", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_cap_pressure_exponent_inv: str = field( + default="{2}", + metadata={ + "name": "phaseCapPressureExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_entry_pressure: str = field( + default="{1}", + metadata={ + "name": "phaseEntryPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class BrooksCoreyRelativePermeability: + class Meta: + name = "BrooksCoreyRelativePermeabilityType" + + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + phase_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "phaseRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "phaseRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class BrooksCoreyStone2RelativePermeability: + class Meta: + name = "BrooksCoreyStone2RelativePermeabilityType" + + gas_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "gasOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "waterOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Co2BrineEzrokhiFluid: + class Meta: + name = "CO2BrineEzrokhiFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Co2BrineEzrokhiThermalFluid: + class Meta: + name = "CO2BrineEzrokhiThermalFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Co2BrinePhillipsFluid: + class Meta: + name = "CO2BrinePhillipsFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Co2BrinePhillipsThermalFluid: + class Meta: + name = "CO2BrinePhillipsThermalFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CarmanKozenyPermeability: + class Meta: + name = "CarmanKozenyPermeabilityType" + + anisotropy: str = field( + default="{1,1,1}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + particle_diameter: str = field( + metadata={ + "name": "particleDiameter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + sphericity: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CellElementRegion: + class Meta: + name = "CellElementRegionType" + + cell_blocks: str = field( + metadata={ + "name": "cellBlocks", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + coarsening_ratio: str = field( + default="0", + metadata={ + "name": "coarseningRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CeramicDamage: + class Meta: + name = "CeramicDamageType" + + compressive_strength: str = field( + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + crack_speed: str = field( + metadata={ + "name": "crackSpeed", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + maximum_strength: str = field( + metadata={ + "name": "maximumStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ChomboIo: + class Meta: + name = "ChomboIOType" + + begin_cycle: str = field( + metadata={ + "name": "beginCycle", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + input_path: str = field( + default="/INVALID_INPUT_PATH", + metadata={ + "name": "inputPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_path: str = field( + metadata={ + "name": "outputPath", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_chombo_pressures: str = field( + default="0", + metadata={ + "name": "useChomboPressures", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + wait_for_input: str = field( + metadata={ + "name": "waitForInput", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositeFunction: + class Meta: + name = "CompositeFunctionType" + + expression: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + function_names: str = field( + default="{}", + metadata={ + "name": "functionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + variable_names: str = field( + default="{}", + metadata={ + "name": "variableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseFluid: + class Meta: + name = "CompositionalMultiphaseFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: str = field( + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: str = field( + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_temperature: str = field( + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + equations_of_state: str = field( + metadata={ + "name": "equationsOfState", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseReservoirPoromechanicsInitialization: + class Meta: + name = "CompositionalMultiphaseReservoirPoromechanicsInitializationType" + + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseStatistics: + class Meta: + name = "CompositionalMultiphaseStatisticsType" + + compute_cflnumbers: str = field( + default="0", + metadata={ + "name": "computeCFLNumbers", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + compute_region_statistics: str = field( + default="1", + metadata={ + "name": "computeRegionStatistics", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + relperm_threshold: str = field( + default="1e-06", + metadata={ + "name": "relpermThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositonalTwoPhaseFluidPengRobinson: + class Meta: + name = "CompositonalTwoPhaseFluidPengRobinsonType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: str = field( + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: str = field( + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_temperature: str = field( + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_volume: str = field( + default="{0}", + metadata={ + "name": "componentCriticalVolume", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositonalTwoPhaseFluidSoaveRedlichKwong: + class Meta: + name = "CompositonalTwoPhaseFluidSoaveRedlichKwongType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: str = field( + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: str = field( + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_temperature: str = field( + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_volume: str = field( + default="{0}", + metadata={ + "name": "componentCriticalVolume", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSinglePhaseFluid: + class Meta: + name = "CompressibleSinglePhaseFluidType" + + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_viscosity: str = field( + metadata={ + "name": "defaultViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + density_model_type: str = field( + default="linear", + metadata={ + "name": "densityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="0", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosity_model_type: str = field( + default="linear", + metadata={ + "name": "viscosityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSolidCarmanKozenyPermeability: + class Meta: + name = "CompressibleSolidCarmanKozenyPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSolidConstantPermeability: + class Meta: + name = "CompressibleSolidConstantPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSolidExponentialDecayPermeability: + class Meta: + name = "CompressibleSolidExponentialDecayPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSolidParallelPlatesPermeability: + class Meta: + name = "CompressibleSolidParallelPlatesPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSolidSlipDependentPermeability: + class Meta: + name = "CompressibleSolidSlipDependentPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompressibleSolidWillisRichardsPermeability: + class Meta: + name = "CompressibleSolidWillisRichardsPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ConstantDiffusion: + class Meta: + name = "ConstantDiffusionType" + + default_phase_diffusivity_multipliers: str = field( + default="{1}", + metadata={ + "name": "defaultPhaseDiffusivityMultipliers", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + diffusivity_components: str = field( + metadata={ + "name": "diffusivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ConstantPermeability: + class Meta: + name = "ConstantPermeabilityType" + + permeability_components: str = field( + metadata={ + "name": "permeabilityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Coulomb: + class Meta: + name = "CoulombType" + + aperture_table_name: str = field( + metadata={ + "name": "apertureTableName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + aperture_tolerance: str = field( + default="1e-09", + metadata={ + "name": "apertureTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cohesion: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + displacement_jump_threshold: str = field( + default="2.22045e-16", + metadata={ + "name": "displacementJumpThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + friction_coefficient: str = field( + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + penalty_stiffness: str = field( + default="0", + metadata={ + "name": "penaltyStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_stiffness: str = field( + default="0", + metadata={ + "name": "shearStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CustomPolarObject: + class Meta: + name = "CustomPolarObjectType" + + center: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + coefficients: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + length_vector: str = field( + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: str = field( + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Cylinder: + class Meta: + name = "CylinderType" + + first_face_center: str = field( + metadata={ + "name": "firstFaceCenter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + inner_radius: str = field( + default="-1", + metadata={ + "name": "innerRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + outer_radius: str = field( + metadata={ + "name": "outerRadius", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + second_face_center: str = field( + metadata={ + "name": "secondFaceCenter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class DamageElasticIsotropic: + class Meta: + name = "DamageElasticIsotropicType" + + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: str = field( + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + critical_strain_energy: str = field( + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: str = field( + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class DamageSpectralElasticIsotropic: + class Meta: + name = "DamageSpectralElasticIsotropicType" + + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: str = field( + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + critical_strain_energy: str = field( + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: str = field( + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class DamageVolDevElasticIsotropic: + class Meta: + name = "DamageVolDevElasticIsotropicType" + + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: str = field( + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + critical_strain_energy: str = field( + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: str = field( + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class DeadOilFluid: + class Meta: + name = "DeadOilFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hydrocarbon_formation_vol_factor_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonFormationVolFactorTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + hydrocarbon_viscosity_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonViscosityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + surface_densities: str = field( + metadata={ + "name": "surfaceDensities", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + table_files: str = field( + default="{}", + metadata={ + "name": "tableFiles", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + water_compressibility: str = field( + default="0", + metadata={ + "name": "waterCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_formation_volume_factor: str = field( + default="0", + metadata={ + "name": "waterFormationVolumeFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_reference_pressure: str = field( + default="0", + metadata={ + "name": "waterReferencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_viscosity: str = field( + default="0", + metadata={ + "name": "waterViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class DelftEgg: + class Meta: + name = "DelftEggType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shape_parameter: str = field( + default="1", + metadata={ + "name": "defaultShapeParameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Dirichlet: + class Meta: + name = "DirichletType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Disc: + class Meta: + name = "DiscType" + + center: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + length_vector: str = field( + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: str = field( + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class DruckerPrager: + class Meta: + name = "DruckerPragerType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_angle: str = field( + default="30", + metadata={ + "name": "defaultDilationAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening_rate: str = field( + default="0", + metadata={ + "name": "defaultHardeningRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ElasticIsotropicPressureDependent: + class Meta: + name = "ElasticIsotropicPressureDependentType" + + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ElasticIsotropic: + class Meta: + name = "ElasticIsotropicType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ElasticOrthotropic: + class Meta: + name = "ElasticOrthotropicType" + + default_c11: str = field( + default="-1", + metadata={ + "name": "defaultC11", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c12: str = field( + default="-1", + metadata={ + "name": "defaultC12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c13: str = field( + default="-1", + metadata={ + "name": "defaultC13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c22: str = field( + default="-1", + metadata={ + "name": "defaultC22", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c23: str = field( + default="-1", + metadata={ + "name": "defaultC23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c33: str = field( + default="-1", + metadata={ + "name": "defaultC33", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c44: str = field( + default="-1", + metadata={ + "name": "defaultC44", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c55: str = field( + default="-1", + metadata={ + "name": "defaultC55", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c66: str = field( + default="-1", + metadata={ + "name": "defaultC66", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e1: str = field( + default="-1", + metadata={ + "name": "defaultE1", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e2: str = field( + default="-1", + metadata={ + "name": "defaultE2", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e3: str = field( + default="-1", + metadata={ + "name": "defaultE3", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g12: str = field( + default="-1", + metadata={ + "name": "defaultG12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g13: str = field( + default="-1", + metadata={ + "name": "defaultG13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g23: str = field( + default="-1", + metadata={ + "name": "defaultG23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu12: str = field( + default="-1", + metadata={ + "name": "defaultNu12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu13: str = field( + default="-1", + metadata={ + "name": "defaultNu13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu23: str = field( + default="-1", + metadata={ + "name": "defaultNu23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ElasticTransverseIsotropic: + class Meta: + name = "ElasticTransverseIsotropicType" + + default_c11: str = field( + default="-1", + metadata={ + "name": "defaultC11", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c13: str = field( + default="-1", + metadata={ + "name": "defaultC13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c33: str = field( + default="-1", + metadata={ + "name": "defaultC33", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c44: str = field( + default="-1", + metadata={ + "name": "defaultC44", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c66: str = field( + default="-1", + metadata={ + "name": "defaultC66", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio_axial_transverse: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatioAxialTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio_transverse: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatioTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus_axial_transverse: str = field( + default="-1", + metadata={ + "name": "defaultShearModulusAxialTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus_axial: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulusAxial", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus_transverse: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulusTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ExponentialDecayPermeability: + class Meta: + name = "ExponentialDecayPermeabilityType" + + empirical_constant: str = field( + metadata={ + "name": "empiricalConstant", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + initial_permeability: str = field( + metadata={ + "name": "initialPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ExtendedDruckerPrager: + class Meta: + name = "ExtendedDruckerPragerType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_ratio: str = field( + default="1", + metadata={ + "name": "defaultDilationRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening: str = field( + default="0", + metadata={ + "name": "defaultHardening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_initial_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultInitialFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_residual_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultResidualFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class FieldSpecification: + class Meta: + name = "FieldSpecificationType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class File: + class Meta: + name = "FileType" + + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + } + ) + + +@dataclass(kw_only=True) +class FiniteElementSpace: + class Meta: + name = "FiniteElementSpaceType" + + formulation: str = field( + default="default", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|SEM", + }, + ) + order: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + use_virtual_elements: str = field( + default="0", + metadata={ + "name": "useVirtualElements", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class FrictionlessContact: + class Meta: + name = "FrictionlessContactType" + + aperture_table_name: str = field( + metadata={ + "name": "apertureTableName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + aperture_tolerance: str = field( + default="1e-09", + metadata={ + "name": "apertureTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + displacement_jump_threshold: str = field( + default="2.22045e-16", + metadata={ + "name": "displacementJumpThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + penalty_stiffness: str = field( + default="0", + metadata={ + "name": "penaltyStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_stiffness: str = field( + default="0", + metadata={ + "name": "shearStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class HaltEvent: + class Meta: + name = "HaltEventType" + + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List[PeriodicEvent] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List[SoloEvent] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_runtime: str = field( + metadata={ + "name": "maxRuntime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class HybridMimeticDiscretization: + class Meta: + name = "HybridMimeticDiscretizationType" + + inner_product_type: str = field( + metadata={ + "name": "innerProductType", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class HydrostaticEquilibrium: + class Meta: + name = "HydrostaticEquilibriumType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component_fraction_vs_elevation_table_names: str = field( + default="{}", + metadata={ + "name": "componentFractionVsElevationTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + datum_elevation: str = field( + metadata={ + "name": "datumElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + datum_pressure: str = field( + metadata={ + "name": "datumPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + elevation_increment_in_hydrostatic_pressure_table: str = field( + default="0.6096", + metadata={ + "name": "elevationIncrementInHydrostaticPressureTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + equilibration_tolerance: str = field( + default="0.001", + metadata={ + "name": "equilibrationTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_phase_name: Optional[str] = field( + default=None, + metadata={ + "name": "initialPhaseName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_number_of_equilibration_iterations: str = field( + default="5", + metadata={ + "name": "maxNumberOfEquilibrationIterations", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature_vs_elevation_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "temperatureVsElevationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class JfunctionCapillaryPressure: + class Meta: + name = "JFunctionCapillaryPressureType" + + non_wetting_intermediate_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "nonWettingIntermediateJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + non_wetting_intermediate_surface_tension: str = field( + default="0", + metadata={ + "name": "nonWettingIntermediateSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + permeability_direction: str = field( + metadata={ + "name": "permeabilityDirection", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|XY|X|Y|Z", + } + ) + permeability_exponent: str = field( + default="0.5", + metadata={ + "name": "permeabilityExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + porosity_exponent: str = field( + default="0.5", + metadata={ + "name": "porosityExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + wetting_intermediate_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingIntermediateJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_intermediate_surface_tension: str = field( + default="0", + metadata={ + "name": "wettingIntermediateSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + wetting_non_wetting_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingNonWettingJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_non_wetting_surface_tension: str = field( + default="0", + metadata={ + "name": "wettingNonWettingSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class LinearIsotropicDispersion: + class Meta: + name = "LinearIsotropicDispersionType" + + longitudinal_dispersivity: str = field( + metadata={ + "name": "longitudinalDispersivity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class LinearSolverParameters: + class Meta: + name = "LinearSolverParametersType" + + amg_aggressive_coarsening_levels: str = field( + default="0", + metadata={ + "name": "amgAggressiveCoarseningLevels", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_aggressive_coarsening_paths: str = field( + default="1", + metadata={ + "name": "amgAggressiveCoarseningPaths", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_aggressive_interp_type: str = field( + default="multipass", + metadata={ + "name": "amgAggressiveInterpType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|extendedIStage2|standardStage2|extendedStage2|multipass|modifiedExtended|modifiedExtendedI|modifiedExtendedE|modifiedMultipass", + }, + ) + amg_coarse_solver: str = field( + default="direct", + metadata={ + "name": "amgCoarseSolver", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|jacobi|l1jacobi|fgs|sgs|l1sgs|chebyshev|direct|bgs", + }, + ) + amg_coarsening_type: str = field( + default="HMIS", + metadata={ + "name": "amgCoarseningType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|CLJP|RugeStueben|Falgout|PMIS|HMIS", + }, + ) + amg_interpolation_max_non_zeros: str = field( + default="4", + metadata={ + "name": "amgInterpolationMaxNonZeros", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_interpolation_type: str = field( + default="extendedI", + metadata={ + "name": "amgInterpolationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|modifiedClassical|direct|multipass|extendedI|standard|extended|directBAMG|modifiedExtended|modifiedExtendedI|modifiedExtendedE", + }, + ) + amg_null_space_type: str = field( + default="constantModes", + metadata={ + "name": "amgNullSpaceType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|constantModes|rigidBodyModes", + }, + ) + amg_num_functions: str = field( + default="1", + metadata={ + "name": "amgNumFunctions", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_num_sweeps: str = field( + default="1", + metadata={ + "name": "amgNumSweeps", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_relax_weight: str = field( + default="1", + metadata={ + "name": "amgRelaxWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + amg_separate_components: str = field( + default="0", + metadata={ + "name": "amgSeparateComponents", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_smoother_type: str = field( + default="l1sgs", + metadata={ + "name": "amgSmootherType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|jacobi|l1jacobi|fgs|bgs|sgs|l1sgs|chebyshev|ilu0|ilut|ic0|ict", + }, + ) + amg_threshold: str = field( + default="0", + metadata={ + "name": "amgThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direct_check_residual: str = field( + default="0", + metadata={ + "name": "directCheckResidual", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_col_perm: str = field( + default="metis", + metadata={ + "name": "directColPerm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|MMD_AtplusA|MMD_AtA|colAMD|metis|parmetis", + }, + ) + direct_equil: str = field( + default="1", + metadata={ + "name": "directEquil", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_iter_ref: str = field( + default="1", + metadata={ + "name": "directIterRef", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_parallel: str = field( + default="1", + metadata={ + "name": "directParallel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_repl_tiny_pivot: str = field( + default="1", + metadata={ + "name": "directReplTinyPivot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_row_perm: str = field( + default="mc64", + metadata={ + "name": "directRowPerm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|mc64", + }, + ) + ilu_fill: str = field( + default="0", + metadata={ + "name": "iluFill", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + ilu_threshold: str = field( + default="0", + metadata={ + "name": "iluThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + krylov_adaptive_tol: str = field( + default="0", + metadata={ + "name": "krylovAdaptiveTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_max_iter: str = field( + default="200", + metadata={ + "name": "krylovMaxIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_max_restart: str = field( + default="200", + metadata={ + "name": "krylovMaxRestart", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_tol: str = field( + default="1e-06", + metadata={ + "name": "krylovTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + krylov_weakest_tol: str = field( + default="0.001", + metadata={ + "name": "krylovWeakestTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + preconditioner_type: str = field( + default="iluk", + metadata={ + "name": "preconditionerType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|jacobi|l1jacobi|fgs|sgs|l1sgs|chebyshev|iluk|ilut|icc|ict|amg|mgr|block|direct|bgs", + }, + ) + solver_type: str = field( + default="direct", + metadata={ + "name": "solverType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|direct|cg|gmres|fgmres|bicgstab|preconditioner", + }, + ) + stop_if_error: str = field( + default="1", + metadata={ + "name": "stopIfError", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + + +@dataclass(kw_only=True) +class ModifiedCamClay: + class Meta: + name = "ModifiedCamClayType" + + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class MultiPhaseConstantThermalConductivity: + class Meta: + name = "MultiPhaseConstantThermalConductivityType" + + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + thermal_conductivity_components: str = field( + metadata={ + "name": "thermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class MultiPhaseVolumeWeightedThermalConductivity: + class Meta: + name = "MultiPhaseVolumeWeightedThermalConductivityType" + + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + phase_thermal_conductivity: str = field( + metadata={ + "name": "phaseThermalConductivity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + rock_thermal_conductivity_components: str = field( + metadata={ + "name": "rockThermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class MultiphasePoromechanicsInitialization: + class Meta: + name = "MultiphasePoromechanicsInitializationType" + + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class MultivariableTableFunction: + class Meta: + name = "MultivariableTableFunctionType" + + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class NonlinearSolverParameters: + class Meta: + name = "NonlinearSolverParametersType" + + allow_non_converged: str = field( + default="0", + metadata={ + "name": "allowNonConverged", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + coupling_type: str = field( + default="FullyImplicit", + metadata={ + "name": "couplingType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|FullyImplicit|Sequential", + }, + ) + line_search_action: str = field( + default="Attempt", + metadata={ + "name": "lineSearchAction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Attempt|Require", + }, + ) + line_search_cut_factor: str = field( + default="0.5", + metadata={ + "name": "lineSearchCutFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + line_search_interpolation_type: str = field( + default="Linear", + metadata={ + "name": "lineSearchInterpolationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Linear|Parabolic", + }, + ) + line_search_max_cuts: str = field( + default="4", + metadata={ + "name": "lineSearchMaxCuts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + line_search_starting_iteration: str = field( + default="0", + metadata={ + "name": "lineSearchStartingIteration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_allowed_residual_norm: str = field( + default="1e+09", + metadata={ + "name": "maxAllowedResidualNorm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_configuration_attempts: str = field( + default="10", + metadata={ + "name": "maxNumConfigurationAttempts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_sub_steps: str = field( + default="10", + metadata={ + "name": "maxSubSteps", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_time_step_cuts: str = field( + default="2", + metadata={ + "name": "maxTimeStepCuts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + min_normalizer: str = field( + default="1e-12", + metadata={ + "name": "minNormalizer", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newton_max_iter: str = field( + default="5", + metadata={ + "name": "newtonMaxIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newton_min_iter: str = field( + default="1", + metadata={ + "name": "newtonMinIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newton_tol: str = field( + default="1e-06", + metadata={ + "name": "newtonTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + nonlinear_acceleration_type: str = field( + default="None", + metadata={ + "name": "nonlinearAccelerationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Aitken", + }, + ) + sequential_convergence_criterion: str = field( + default="ResidualNorm", + metadata={ + "name": "sequentialConvergenceCriterion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|ResidualNorm|NumberOfNonlinearIterations|SolutionIncrements", + }, + ) + subcycling: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + time_step_cut_factor: str = field( + default="0.5", + metadata={ + "name": "timeStepCutFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_decrease_factor: str = field( + default="0.5", + metadata={ + "name": "timeStepDecreaseFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_decrease_iter_limit: str = field( + default="0.7", + metadata={ + "name": "timeStepDecreaseIterLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_increase_factor: str = field( + default="2", + metadata={ + "name": "timeStepIncreaseFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_increase_iter_limit: str = field( + default="0.4", + metadata={ + "name": "timeStepIncreaseIterLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + norm_type: str = field( + default="Linfinity", + metadata={ + "name": "normType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Linfinity|L2", + }, + ) + + +@dataclass(kw_only=True) +class NullModel: + class Meta: + name = "NullModelType" + + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Pml: + class Meta: + name = "PMLType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + reflectivity: str = field( + default="0.001", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + thickness_max_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "thicknessMaxXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + thickness_min_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "thicknessMinXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + wave_speed_max_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "waveSpeedMaxXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + wave_speed_min_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "waveSpeedMinXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_max: str = field( + default="{3.40282e+38,3.40282e+38,3.40282e+38}", + metadata={ + "name": "xMax", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_min: str = field( + default="{-3.40282e+38,-3.40282e+38,-3.40282e+38}", + metadata={ + "name": "xMin", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Pvtdriver: + class Meta: + name = "PVTDriverType" + + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + feed_composition: str = field( + metadata={ + "name": "feedComposition", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + fluid: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_compressibility: str = field( + default="0", + metadata={ + "name": "outputCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_phase_composition: str = field( + default="0", + metadata={ + "name": "outputPhaseComposition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + pressure_control: str = field( + metadata={ + "name": "pressureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + temperature_control: str = field( + metadata={ + "name": "temperatureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PackCollection: + class Meta: + name = "PackCollectionType" + + disable_coord_collection: str = field( + default="0", + metadata={ + "name": "disableCoordCollection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + field_name: str = field( + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + object_path: str = field( + metadata={ + "name": "objectPath", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + only_on_set_change: str = field( + default="0", + metadata={ + "name": "onlyOnSetChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + set_names: str = field( + default="{}", + metadata={ + "name": "setNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ParallelPlatesPermeability: + class Meta: + name = "ParallelPlatesPermeabilityType" + + transversal_permeability: str = field( + default="-1", + metadata={ + "name": "transversalPermeability", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Parameter: + class Meta: + name = "ParameterType" + + value: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ParticleFluid: + class Meta: + name = "ParticleFluidType" + + collision_alpha: str = field( + default="1.27", + metadata={ + "name": "collisionAlpha", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + collision_beta: str = field( + default="1.5", + metadata={ + "name": "collisionBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + fluid_viscosity: str = field( + default="0.001", + metadata={ + "name": "fluidViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + hindered_settling_coefficient: str = field( + default="5.9", + metadata={ + "name": "hinderedSettlingCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_collisional_slip: str = field( + default="0", + metadata={ + "name": "isCollisionalSlip", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + particle_settling_model: str = field( + metadata={ + "name": "particleSettlingModel", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|Stokes|Intermediate|Turbulence", + } + ) + proppant_density: str = field( + default="1400", + metadata={ + "name": "proppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: str = field( + default="0.0002", + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + slip_concentration: str = field( + default="0.1", + metadata={ + "name": "slipConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + sphericity: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ParticleMesh: + class Meta: + name = "ParticleMeshType" + + header_file: str = field( + metadata={ + "name": "headerFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + } + ) + particle_block_names: str = field( + metadata={ + "name": "particleBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + particle_file: str = field( + metadata={ + "name": "particleFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + } + ) + particle_types: str = field( + metadata={ + "name": "particleTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ParticleRegion: + class Meta: + name = "ParticleRegionType" + + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + particle_blocks: str = field( + default="{}", + metadata={ + "name": "particleBlocks", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PerfectlyPlastic: + class Meta: + name = "PerfectlyPlasticType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_yield_stress: str = field( + default="1.79769e+308", + metadata={ + "name": "defaultYieldStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Perforation: + class Meta: + name = "PerforationType" + + distance_from_head: str = field( + metadata={ + "name": "distanceFromHead", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + skin_factor: str = field( + default="0", + metadata={ + "name": "skinFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + transmissibility: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PermeabilityBase: + class Meta: + name = "PermeabilityBaseType" + + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousDamageElasticIsotropic: + class Meta: + name = "PorousDamageElasticIsotropicType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousDamageSpectralElasticIsotropic: + class Meta: + name = "PorousDamageSpectralElasticIsotropicType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousDamageVolDevElasticIsotropic: + class Meta: + name = "PorousDamageVolDevElasticIsotropicType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousDelftEgg: + class Meta: + name = "PorousDelftEggType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousDruckerPrager: + class Meta: + name = "PorousDruckerPragerType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousElasticIsotropic: + class Meta: + name = "PorousElasticIsotropicType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousElasticOrthotropic: + class Meta: + name = "PorousElasticOrthotropicType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousElasticTransverseIsotropic: + class Meta: + name = "PorousElasticTransverseIsotropicType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousExtendedDruckerPrager: + class Meta: + name = "PorousExtendedDruckerPragerType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousModifiedCamClay: + class Meta: + name = "PorousModifiedCamClayType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousViscoDruckerPrager: + class Meta: + name = "PorousViscoDruckerPragerType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousViscoExtendedDruckerPrager: + class Meta: + name = "PorousViscoExtendedDruckerPragerType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PorousViscoModifiedCamClay: + class Meta: + name = "PorousViscoModifiedCamClayType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PressurePorosity: + class Meta: + name = "PressurePorosityType" + + compressibility: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_reference_porosity: str = field( + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + reference_pressure: str = field( + metadata={ + "name": "referencePressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ProppantPermeability: + class Meta: + name = "ProppantPermeabilityType" + + max_proppant_concentration: str = field( + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + proppant_diameter: str = field( + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ProppantPorosity: + class Meta: + name = "ProppantPorosityType" + + default_reference_porosity: str = field( + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + max_proppant_concentration: str = field( + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ProppantSlurryFluid: + class Meta: + name = "ProppantSlurryFluidType" + + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_component_density: str = field( + default="{0}", + metadata={ + "name": "defaultComponentDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + default_component_viscosity: str = field( + default="{0}", + metadata={ + "name": "defaultComponentViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + default_compressibility: str = field( + default="{0}", + metadata={ + "name": "defaultCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + flow_behavior_index: str = field( + default="{0}", + metadata={ + "name": "flowBehaviorIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + flow_consistency_index: str = field( + default="{0}", + metadata={ + "name": "flowConsistencyIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="100000", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_proppant_density: str = field( + default="1400", + metadata={ + "name": "referenceProppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ProppantSolidProppantPermeability: + class Meta: + name = "ProppantSolidProppantPermeabilityType" + + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Python: + class Meta: + name = "PythonType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ReactiveBrineThermal: + class Meta: + name = "ReactiveBrineThermalType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ReactiveBrine: + class Meta: + name = "ReactiveBrineType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ReactiveFluidDriver: + class Meta: + name = "ReactiveFluidDriverType" + + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + feed_composition: str = field( + metadata={ + "name": "feedComposition", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + fluid: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + pressure_control: str = field( + metadata={ + "name": "pressureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + temperature_control: str = field( + metadata={ + "name": "temperatureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Rectangle: + class Meta: + name = "RectangleType" + + dimensions: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + length_vector: str = field( + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + origin: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: str = field( + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class RelpermDriver: + class Meta: + name = "RelpermDriverType" + + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + relperm: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Restart: + class Meta: + name = "RestartType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Run: + class Meta: + name = "RunType" + + args: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + auto_partition: Optional[str] = field( + default=None, + metadata={ + "name": "autoPartition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + mesh_sizes: str = field( + default="{0}", + metadata={ + "name": "meshSizes", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + nodes: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + scale_list: str = field( + default="{0}", + metadata={ + "name": "scaleList", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + scaling: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + tasks_per_node: str = field( + metadata={ + "name": "tasksPerNode", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + threads_per_task: str = field( + default="0", + metadata={ + "name": "threadsPerTask", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + time_limit: str = field( + default="0", + metadata={ + "name": "timeLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + + +@dataclass(kw_only=True) +class Silo: + class Meta: + name = "SiloType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + field_names: str = field( + default="{}", + metadata={ + "name": "fieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + only_plot_specified_field_names: str = field( + default="0", + metadata={ + "name": "onlyPlotSpecifiedFieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_file_root: str = field( + default="plot", + metadata={ + "name": "plotFileRoot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_cell_element_mesh: str = field( + default="1", + metadata={ + "name": "writeCellElementMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_edge_mesh: str = field( + default="0", + metadata={ + "name": "writeEdgeMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_femfaces: str = field( + default="0", + metadata={ + "name": "writeFEMFaces", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_face_element_mesh: str = field( + default="1", + metadata={ + "name": "writeFaceElementMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseConstantThermalConductivity: + class Meta: + name = "SinglePhaseConstantThermalConductivityType" + + thermal_conductivity_components: str = field( + metadata={ + "name": "thermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhasePoromechanicsInitialization: + class Meta: + name = "SinglePhasePoromechanicsInitializationType" + + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseReservoirPoromechanicsInitialization: + class Meta: + name = "SinglePhaseReservoirPoromechanicsInitializationType" + + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseStatistics: + class Meta: + name = "SinglePhaseStatisticsType" + + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SlipDependentPermeability: + class Meta: + name = "SlipDependentPermeabilityType" + + initial_permeability: str = field( + metadata={ + "name": "initialPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + max_perm_multiplier: str = field( + metadata={ + "name": "maxPermMultiplier", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + shear_disp_threshold: str = field( + metadata={ + "name": "shearDispThreshold", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidInternalEnergy: + class Meta: + name = "SolidInternalEnergyType" + + reference_internal_energy: str = field( + metadata={ + "name": "referenceInternalEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + reference_temperature: str = field( + metadata={ + "name": "referenceTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + volumetric_heat_capacity: str = field( + metadata={ + "name": "volumetricHeatCapacity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsStateReset: + class Meta: + name = "SolidMechanicsStateResetType" + + disable_inelasticity: str = field( + default="0", + metadata={ + "name": "disableInelasticity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reset_displacements: str = field( + default="1", + metadata={ + "name": "resetDisplacements", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsStatistics: + class Meta: + name = "SolidMechanicsStatisticsType" + + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SourceFlux: + class Meta: + name = "SourceFluxType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SurfaceElementRegion: + class Meta: + name = "SurfaceElementRegionType" + + default_aperture: str = field( + metadata={ + "name": "defaultAperture", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + face_block: str = field( + default="FractureSubRegion", + metadata={ + "name": "faceBlock", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + sub_region_type: str = field( + default="faceElement", + metadata={ + "name": "subRegionType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|faceElement|embeddedElement", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SymbolicFunction: + class Meta: + name = "SymbolicFunctionType" + + expression: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + variable_names: str = field( + metadata={ + "name": "variableNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TableCapillaryPressure: + class Meta: + name = "TableCapillaryPressureType" + + non_wetting_intermediate_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "nonWettingIntermediateCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + wetting_intermediate_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingIntermediateCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_non_wetting_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingNonWettingCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TableFunction: + class Meta: + name = "TableFunctionType" + + coordinate_files: str = field( + default="{}", + metadata={ + "name": "coordinateFiles", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + coordinates: str = field( + default="{0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + interpolation: str = field( + default="linear", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|linear|nearest|upper|lower", + }, + ) + values: str = field( + default="{0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + voxel_file: Optional[str] = field( + default=None, + metadata={ + "name": "voxelFile", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TableRelativePermeabilityHysteresis: + class Meta: + name = "TableRelativePermeabilityHysteresisType" + + drainage_non_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageNonWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + drainage_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + drainage_wetting_non_wetting_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageWettingNonWettingRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + imbibition_non_wetting_rel_perm_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "imbibitionNonWettingRelPermTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + imbibition_wetting_rel_perm_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "imbibitionWettingRelPermTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + jerauld_parameter_a: str = field( + default="0.1", + metadata={ + "name": "jerauldParameterA", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + jerauld_parameter_b: str = field( + default="0", + metadata={ + "name": "jerauldParameterB", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + killough_curvature_parameter: str = field( + default="1", + metadata={ + "name": "killoughCurvatureParameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + three_phase_interpolator: str = field( + default="BAKER", + metadata={ + "name": "threePhaseInterpolator", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|BAKER|STONEII", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TableRelativePermeability: + class Meta: + name = "TableRelativePermeabilityType" + + non_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "nonWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + three_phase_interpolator: str = field( + default="BAKER", + metadata={ + "name": "threePhaseInterpolator", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|BAKER|STONEII", + }, + ) + wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "wettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + wetting_non_wetting_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "wettingNonWettingRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ThermalCompressibleSinglePhaseFluid: + class Meta: + name = "ThermalCompressibleSinglePhaseFluidType" + + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_viscosity: str = field( + metadata={ + "name": "defaultViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + density_model_type: str = field( + default="linear", + metadata={ + "name": "densityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + internal_energy_model_type: str = field( + default="linear", + metadata={ + "name": "internalEnergyModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_internal_energy: str = field( + default="0.001", + metadata={ + "name": "referenceInternalEnergy", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="0", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_temperature: str = field( + default="0", + metadata={ + "name": "referenceTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + specific_heat_capacity: str = field( + default="0", + metadata={ + "name": "specificHeatCapacity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + thermal_expansion_coeff: str = field( + default="0", + metadata={ + "name": "thermalExpansionCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosity_model_type: str = field( + default="linear", + metadata={ + "name": "viscosityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ThickPlane: + class Meta: + name = "ThickPlaneType" + + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + origin: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + thickness: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TimeHistory: + class Meta: + name = "TimeHistoryType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + filename: str = field( + default="TimeHistory", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + format: str = field( + default="hdf", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + sources: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Traction: + class Meta: + name = "TractionType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + input_stress: str = field( + default="{0,0,0,0,0,0}", + metadata={ + "name": "inputStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){5}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + traction_type: str = field( + default="vector", + metadata={ + "name": "tractionType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|vector|normal|stress", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TriaxialDriver: + class Meta: + name = "TriaxialDriverType" + + axial_control: str = field( + metadata={ + "name": "axialControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + initial_stress: str = field( + metadata={ + "name": "initialStress", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + material: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + mode: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|mixedControl|strainControl|stressControl", + } + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + radial_control: str = field( + metadata={ + "name": "radialControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class TwoPointFluxApproximation: + class Meta: + name = "TwoPointFluxApproximationType" + + area_rel_tol: str = field( + default="1e-08", + metadata={ + "name": "areaRelTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + mean_perm_coefficient: str = field( + default="1", + metadata={ + "name": "meanPermCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + upwinding_scheme: str = field( + default="PPU", + metadata={ + "name": "upwindingScheme", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|PPU|C1PPU|IHU", + }, + ) + use_pedfm: str = field( + default="0", + metadata={ + "name": "usePEDFM", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Vtk: + class Meta: + name = "VTKType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + field_names: str = field( + default="{}", + metadata={ + "name": "fieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + format: str = field( + default="binary", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|binary|ascii", + }, + ) + level_names: str = field( + default="{}", + metadata={ + "name": "levelNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + only_plot_specified_field_names: str = field( + default="0", + metadata={ + "name": "onlyPlotSpecifiedFieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_region_type: str = field( + default="all", + metadata={ + "name": "outputRegionType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|cell|well|surface|particle|all", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_file_root: str = field( + default="VTK", + metadata={ + "name": "plotFileRoot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_femfaces: str = field( + default="0", + metadata={ + "name": "writeFEMFaces", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_ghost_cells: str = field( + default="0", + metadata={ + "name": "writeGhostCells", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class VanGenuchtenBakerRelativePermeability: + class Meta: + name = "VanGenuchtenBakerRelativePermeabilityType" + + gas_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "gasOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "waterOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class VanGenuchtenCapillaryPressure: + class Meta: + name = "VanGenuchtenCapillaryPressureType" + + cap_pressure_epsilon: str = field( + default="1e-06", + metadata={ + "name": "capPressureEpsilon", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_cap_pressure_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "phaseCapPressureExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_cap_pressure_multiplier: str = field( + default="{1}", + metadata={ + "name": "phaseCapPressureMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class VanGenuchtenStone2RelativePermeability: + class Meta: + name = "VanGenuchtenStone2RelativePermeabilityType" + + gas_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "gasOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "waterOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ViscoDruckerPrager: + class Meta: + name = "ViscoDruckerPragerType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_angle: str = field( + default="30", + metadata={ + "name": "defaultDilationAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening_rate: str = field( + default="0", + metadata={ + "name": "defaultHardeningRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: str = field( + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ViscoExtendedDruckerPrager: + class Meta: + name = "ViscoExtendedDruckerPragerType" + + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_ratio: str = field( + default="1", + metadata={ + "name": "defaultDilationRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening: str = field( + default="0", + metadata={ + "name": "defaultHardening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_initial_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultInitialFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_residual_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultResidualFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: str = field( + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ViscoModifiedCamClay: + class Meta: + name = "ViscoModifiedCamClayType" + + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: str = field( + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class WellControls: + class Meta: + name = "WellControlsType" + + control: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|BHP|phaseVolRate|totalVolRate|uninitialized", + } + ) + enable_crossflow: str = field( + default="1", + metadata={ + "name": "enableCrossflow", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_pressure_coefficient: str = field( + default="0.1", + metadata={ + "name": "initialPressureCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + injection_stream: str = field( + default="{-1}", + metadata={ + "name": "injectionStream", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + injection_temperature: str = field( + default="-1", + metadata={ + "name": "injectionTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reference_elevation: str = field( + metadata={ + "name": "referenceElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + status_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "statusTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + surface_pressure: str = field( + default="0", + metadata={ + "name": "surfacePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + surface_temperature: str = field( + default="0", + metadata={ + "name": "surfaceTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_bhp: str = field( + default="0", + metadata={ + "name": "targetBHP", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_bhptable_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetBHPTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_phase_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetPhaseName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_phase_rate: str = field( + default="0", + metadata={ + "name": "targetPhaseRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_rate_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetPhaseRateTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_total_rate: str = field( + default="0", + metadata={ + "name": "targetTotalRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_total_rate_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetTotalRateTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + type_value: str = field( + metadata={ + "name": "type", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|producer|injector", + } + ) + use_surface_conditions: str = field( + default="0", + metadata={ + "name": "useSurfaceConditions", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class WellElementRegion: + class Meta: + name = "WellElementRegionType" + + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class WillisRichardsPermeability: + class Meta: + name = "WillisRichardsPermeabilityType" + + dilation_coefficient: str = field( + metadata={ + "name": "dilationCoefficient", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + max_frac_aperture: str = field( + metadata={ + "name": "maxFracAperture", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + ref_closure_stress: str = field( + metadata={ + "name": "refClosureStress", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class AcousticElasticSem: + class Meta: + name = "AcousticElasticSEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + acoustic_solver_name: str = field( + metadata={ + "name": "acousticSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + elastic_solver_name: str = field( + metadata={ + "name": "elasticSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class AcousticFirstOrderSem: + class Meta: + name = "AcousticFirstOrderSEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class AcousticSem: + class Meta: + name = "AcousticSEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class AcousticVtisem: + class Meta: + name = "AcousticVTISEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseFvm: + class Meta: + name = "CompositionalMultiphaseFVMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cont_multiplier_dbc: str = field( + default="0.5", + metadata={ + "name": "contMultiplierDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + continuation_dbc: str = field( + default="1", + metadata={ + "name": "continuationDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + kappamin_dbc: str = field( + default="1e-20", + metadata={ + "name": "kappaminDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="0.5", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_temperature_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativeTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_comp_dens_change: str = field( + default="1", + metadata={ + "name": "maxSequentialCompDensChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_comp_dens: str = field( + default="1e-10", + metadata={ + "name": "minCompDens", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + miscible_dbc: str = field( + default="0", + metadata={ + "name": "miscibleDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + omega_dbc: str = field( + default="1", + metadata={ + "name": "omegaDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + scaling_type: str = field( + default="Global", + metadata={ + "name": "scalingType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Global|Local", + }, + ) + solution_change_scaling_factor: str = field( + default="0.5", + metadata={ + "name": "solutionChangeScalingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_flow_cfl: str = field( + default="-1", + metadata={ + "name": "targetFlowCFL", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_vol_fraction_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetPhaseVolFractionChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + target_relative_pressure_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativePressureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_relative_temperature_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativeTemperatureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + use_dbc: str = field( + default="0", + metadata={ + "name": "useDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_simple_accumulation: str = field( + default="1", + metadata={ + "name": "useSimpleAccumulation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_total_mass_equation: str = field( + default="1", + metadata={ + "name": "useTotalMassEquation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseHybridFvm: + class Meta: + name = "CompositionalMultiphaseHybridFVMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="0.5", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_temperature_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativeTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_comp_dens_change: str = field( + default="1", + metadata={ + "name": "maxSequentialCompDensChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_comp_dens: str = field( + default="1e-10", + metadata={ + "name": "minCompDens", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + solution_change_scaling_factor: str = field( + default="0.5", + metadata={ + "name": "solutionChangeScalingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_flow_cfl: str = field( + default="-1", + metadata={ + "name": "targetFlowCFL", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_vol_fraction_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetPhaseVolFractionChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + target_relative_pressure_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativePressureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_relative_temperature_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativeTemperatureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_simple_accumulation: str = field( + default="1", + metadata={ + "name": "useSimpleAccumulation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_total_mass_equation: str = field( + default="1", + metadata={ + "name": "useTotalMassEquation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseReservoirPoromechanics: + class Meta: + name = "CompositionalMultiphaseReservoirPoromechanicsType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reservoir_and_wells_solver_name: str = field( + metadata={ + "name": "reservoirAndWellsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + stabilization_multiplier: str = field( + default="1", + metadata={ + "name": "stabilizationMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_region_names: str = field( + default="{}", + metadata={ + "name": "stabilizationRegionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + stabilization_type: str = field( + default="None", + metadata={ + "name": "stabilizationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Global|Local", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseReservoir: + class Meta: + name = "CompositionalMultiphaseReservoirType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class CompositionalMultiphaseWell: + class Meta: + name = "CompositionalMultiphaseWellType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + well_controls: List[WellControls] = field( + default_factory=list, + metadata={ + "name": "WellControls", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="1", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="1", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Constitutive: + class Meta: + name = "ConstitutiveType" + + biot_porosity: List[BiotPorosity] = field( + default_factory=list, + metadata={ + "name": "BiotPorosity", + "type": "Element", + "namespace": "", + }, + ) + black_oil_fluid: List[BlackOilFluid] = field( + default_factory=list, + metadata={ + "name": "BlackOilFluid", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_baker_relative_permeability: List[ + BrooksCoreyBakerRelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyBakerRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_capillary_pressure: List[BrooksCoreyCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_relative_permeability: List[BrooksCoreyRelativePermeability] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_stone2_relative_permeability: List[ + BrooksCoreyStone2RelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyStone2RelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_ezrokhi_fluid: List[Co2BrineEzrokhiFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrineEzrokhiFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_ezrokhi_thermal_fluid: List[Co2BrineEzrokhiThermalFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrineEzrokhiThermalFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_phillips_fluid: List[Co2BrinePhillipsFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrinePhillipsFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_phillips_thermal_fluid: List[Co2BrinePhillipsThermalFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrinePhillipsThermalFluid", + "type": "Element", + "namespace": "", + }, + ) + carman_kozeny_permeability: List[CarmanKozenyPermeability] = field( + default_factory=list, + metadata={ + "name": "CarmanKozenyPermeability", + "type": "Element", + "namespace": "", + }, + ) + ceramic_damage: List[CeramicDamage] = field( + default_factory=list, + metadata={ + "name": "CeramicDamage", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_fluid: List[CompositionalMultiphaseFluid] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseFluid", + "type": "Element", + "namespace": "", + }, + ) + compositonal_two_phase_fluid_peng_robinson: List[ + CompositonalTwoPhaseFluidPengRobinson + ] = field( + default_factory=list, + metadata={ + "name": "CompositonalTwoPhaseFluidPengRobinson", + "type": "Element", + "namespace": "", + }, + ) + compositonal_two_phase_fluid_soave_redlich_kwong: List[ + CompositonalTwoPhaseFluidSoaveRedlichKwong + ] = field( + default_factory=list, + metadata={ + "name": "CompositonalTwoPhaseFluidSoaveRedlichKwong", + "type": "Element", + "namespace": "", + }, + ) + compressible_single_phase_fluid: List[CompressibleSinglePhaseFluid] = field( + default_factory=list, + metadata={ + "name": "CompressibleSinglePhaseFluid", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_carman_kozeny_permeability: List[ + CompressibleSolidCarmanKozenyPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidCarmanKozenyPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_constant_permeability: List[ + CompressibleSolidConstantPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidConstantPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_exponential_decay_permeability: List[ + CompressibleSolidExponentialDecayPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidExponentialDecayPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_parallel_plates_permeability: List[ + CompressibleSolidParallelPlatesPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidParallelPlatesPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_slip_dependent_permeability: List[ + CompressibleSolidSlipDependentPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidSlipDependentPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_willis_richards_permeability: List[ + CompressibleSolidWillisRichardsPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidWillisRichardsPermeability", + "type": "Element", + "namespace": "", + }, + ) + constant_diffusion: List[ConstantDiffusion] = field( + default_factory=list, + metadata={ + "name": "ConstantDiffusion", + "type": "Element", + "namespace": "", + }, + ) + constant_permeability: List[ConstantPermeability] = field( + default_factory=list, + metadata={ + "name": "ConstantPermeability", + "type": "Element", + "namespace": "", + }, + ) + coulomb: List[Coulomb] = field( + default_factory=list, + metadata={ + "name": "Coulomb", + "type": "Element", + "namespace": "", + }, + ) + damage_elastic_isotropic: List[DamageElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "DamageElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + damage_spectral_elastic_isotropic: List[DamageSpectralElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "DamageSpectralElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + damage_vol_dev_elastic_isotropic: List[DamageVolDevElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "DamageVolDevElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + dead_oil_fluid: List[DeadOilFluid] = field( + default_factory=list, + metadata={ + "name": "DeadOilFluid", + "type": "Element", + "namespace": "", + }, + ) + delft_egg: List[DelftEgg] = field( + default_factory=list, + metadata={ + "name": "DelftEgg", + "type": "Element", + "namespace": "", + }, + ) + drucker_prager: List[DruckerPrager] = field( + default_factory=list, + metadata={ + "name": "DruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + elastic_isotropic: List[ElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "ElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + elastic_isotropic_pressure_dependent: List[ElasticIsotropicPressureDependent] = ( + field( + default_factory=list, + metadata={ + "name": "ElasticIsotropicPressureDependent", + "type": "Element", + "namespace": "", + }, + ) + ) + elastic_orthotropic: List[ElasticOrthotropic] = field( + default_factory=list, + metadata={ + "name": "ElasticOrthotropic", + "type": "Element", + "namespace": "", + }, + ) + elastic_transverse_isotropic: List[ElasticTransverseIsotropic] = field( + default_factory=list, + metadata={ + "name": "ElasticTransverseIsotropic", + "type": "Element", + "namespace": "", + }, + ) + exponential_decay_permeability: List[ExponentialDecayPermeability] = field( + default_factory=list, + metadata={ + "name": "ExponentialDecayPermeability", + "type": "Element", + "namespace": "", + }, + ) + extended_drucker_prager: List[ExtendedDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "ExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + frictionless_contact: List[FrictionlessContact] = field( + default_factory=list, + metadata={ + "name": "FrictionlessContact", + "type": "Element", + "namespace": "", + }, + ) + jfunction_capillary_pressure: List[JfunctionCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "JFunctionCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + linear_isotropic_dispersion: List[LinearIsotropicDispersion] = field( + default_factory=list, + metadata={ + "name": "LinearIsotropicDispersion", + "type": "Element", + "namespace": "", + }, + ) + modified_cam_clay: List[ModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "ModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + multi_phase_constant_thermal_conductivity: List[ + MultiPhaseConstantThermalConductivity + ] = field( + default_factory=list, + metadata={ + "name": "MultiPhaseConstantThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + multi_phase_volume_weighted_thermal_conductivity: List[ + MultiPhaseVolumeWeightedThermalConductivity + ] = field( + default_factory=list, + metadata={ + "name": "MultiPhaseVolumeWeightedThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + null_model: List[NullModel] = field( + default_factory=list, + metadata={ + "name": "NullModel", + "type": "Element", + "namespace": "", + }, + ) + parallel_plates_permeability: List[ParallelPlatesPermeability] = field( + default_factory=list, + metadata={ + "name": "ParallelPlatesPermeability", + "type": "Element", + "namespace": "", + }, + ) + particle_fluid: List[ParticleFluid] = field( + default_factory=list, + metadata={ + "name": "ParticleFluid", + "type": "Element", + "namespace": "", + }, + ) + perfectly_plastic: List[PerfectlyPlastic] = field( + default_factory=list, + metadata={ + "name": "PerfectlyPlastic", + "type": "Element", + "namespace": "", + }, + ) + permeability_base: List[PermeabilityBase] = field( + default_factory=list, + metadata={ + "name": "PermeabilityBase", + "type": "Element", + "namespace": "", + }, + ) + porous_damage_elastic_isotropic: List[PorousDamageElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "PorousDamageElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_damage_spectral_elastic_isotropic: List[ + PorousDamageSpectralElasticIsotropic + ] = field( + default_factory=list, + metadata={ + "name": "PorousDamageSpectralElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_damage_vol_dev_elastic_isotropic: List[ + PorousDamageVolDevElasticIsotropic + ] = field( + default_factory=list, + metadata={ + "name": "PorousDamageVolDevElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_delft_egg: List[PorousDelftEgg] = field( + default_factory=list, + metadata={ + "name": "PorousDelftEgg", + "type": "Element", + "namespace": "", + }, + ) + porous_drucker_prager: List[PorousDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "PorousDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_isotropic: List[PorousElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "PorousElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_orthotropic: List[PorousElasticOrthotropic] = field( + default_factory=list, + metadata={ + "name": "PorousElasticOrthotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_transverse_isotropic: List[PorousElasticTransverseIsotropic] = field( + default_factory=list, + metadata={ + "name": "PorousElasticTransverseIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_extended_drucker_prager: List[PorousExtendedDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "PorousExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_modified_cam_clay: List[PorousModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "PorousModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + porous_visco_drucker_prager: List[PorousViscoDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "PorousViscoDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_visco_extended_drucker_prager: List[PorousViscoExtendedDruckerPrager] = ( + field( + default_factory=list, + metadata={ + "name": "PorousViscoExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + ) + porous_visco_modified_cam_clay: List[PorousViscoModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "PorousViscoModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + pressure_porosity: List[PressurePorosity] = field( + default_factory=list, + metadata={ + "name": "PressurePorosity", + "type": "Element", + "namespace": "", + }, + ) + proppant_permeability: List[ProppantPermeability] = field( + default_factory=list, + metadata={ + "name": "ProppantPermeability", + "type": "Element", + "namespace": "", + }, + ) + proppant_porosity: List[ProppantPorosity] = field( + default_factory=list, + metadata={ + "name": "ProppantPorosity", + "type": "Element", + "namespace": "", + }, + ) + proppant_slurry_fluid: List[ProppantSlurryFluid] = field( + default_factory=list, + metadata={ + "name": "ProppantSlurryFluid", + "type": "Element", + "namespace": "", + }, + ) + proppant_solid_proppant_permeability: List[ProppantSolidProppantPermeability] = ( + field( + default_factory=list, + metadata={ + "name": "ProppantSolidProppantPermeability", + "type": "Element", + "namespace": "", + }, + ) + ) + reactive_brine: List[ReactiveBrine] = field( + default_factory=list, + metadata={ + "name": "ReactiveBrine", + "type": "Element", + "namespace": "", + }, + ) + reactive_brine_thermal: List[ReactiveBrineThermal] = field( + default_factory=list, + metadata={ + "name": "ReactiveBrineThermal", + "type": "Element", + "namespace": "", + }, + ) + single_phase_constant_thermal_conductivity: List[ + SinglePhaseConstantThermalConductivity + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseConstantThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + slip_dependent_permeability: List[SlipDependentPermeability] = field( + default_factory=list, + metadata={ + "name": "SlipDependentPermeability", + "type": "Element", + "namespace": "", + }, + ) + solid_internal_energy: List[SolidInternalEnergy] = field( + default_factory=list, + metadata={ + "name": "SolidInternalEnergy", + "type": "Element", + "namespace": "", + }, + ) + table_capillary_pressure: List[TableCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "TableCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + table_relative_permeability: List[TableRelativePermeability] = field( + default_factory=list, + metadata={ + "name": "TableRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + table_relative_permeability_hysteresis: List[ + TableRelativePermeabilityHysteresis + ] = field( + default_factory=list, + metadata={ + "name": "TableRelativePermeabilityHysteresis", + "type": "Element", + "namespace": "", + }, + ) + thermal_compressible_single_phase_fluid: List[ + ThermalCompressibleSinglePhaseFluid + ] = field( + default_factory=list, + metadata={ + "name": "ThermalCompressibleSinglePhaseFluid", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_baker_relative_permeability: List[ + VanGenuchtenBakerRelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenBakerRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_capillary_pressure: List[VanGenuchtenCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_stone2_relative_permeability: List[ + VanGenuchtenStone2RelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenStone2RelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + visco_drucker_prager: List[ViscoDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "ViscoDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + visco_extended_drucker_prager: List[ViscoExtendedDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "ViscoExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + visco_modified_cam_clay: List[ViscoModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "ViscoModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + willis_richards_permeability: List[WillisRichardsPermeability] = field( + default_factory=list, + metadata={ + "name": "WillisRichardsPermeability", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class ElasticFirstOrderSem: + class Meta: + name = "ElasticFirstOrderSEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ElasticSem: + class Meta: + name = "ElasticSEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + source_force: str = field( + default="{0,0,0}", + metadata={ + "name": "sourceForce", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + source_moment: str = field( + default="{1,1,1,0,0,0}", + metadata={ + "name": "sourceMoment", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){5}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ElementRegions: + class Meta: + name = "ElementRegionsType" + + cell_element_region: List[CellElementRegion] = field( + default_factory=list, + metadata={ + "name": "CellElementRegion", + "type": "Element", + "namespace": "", + }, + ) + surface_element_region: List[SurfaceElementRegion] = field( + default_factory=list, + metadata={ + "name": "SurfaceElementRegion", + "type": "Element", + "namespace": "", + }, + ) + well_element_region: List[WellElementRegion] = field( + default_factory=list, + metadata={ + "name": "WellElementRegion", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class EmbeddedSurfaceGenerator: + class Meta: + name = "EmbeddedSurfaceGeneratorType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + fracture_region: str = field( + default="FractureRegion", + metadata={ + "name": "fractureRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mpi_comm_order: str = field( + default="0", + metadata={ + "name": "mpiCommOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_objects: str = field( + metadata={ + "name": "targetObjects", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class FieldSpecifications: + class Meta: + name = "FieldSpecificationsType" + + aquifer: List[Aquifer] = field( + default_factory=list, + metadata={ + "name": "Aquifer", + "type": "Element", + "namespace": "", + }, + ) + dirichlet: List[Dirichlet] = field( + default_factory=list, + metadata={ + "name": "Dirichlet", + "type": "Element", + "namespace": "", + }, + ) + field_specification: List[FieldSpecification] = field( + default_factory=list, + metadata={ + "name": "FieldSpecification", + "type": "Element", + "namespace": "", + }, + ) + hydrostatic_equilibrium: List[HydrostaticEquilibrium] = field( + default_factory=list, + metadata={ + "name": "HydrostaticEquilibrium", + "type": "Element", + "namespace": "", + }, + ) + pml: List[Pml] = field( + default_factory=list, + metadata={ + "name": "PML", + "type": "Element", + "namespace": "", + }, + ) + source_flux: List[SourceFlux] = field( + default_factory=list, + metadata={ + "name": "SourceFlux", + "type": "Element", + "namespace": "", + }, + ) + traction: List[Traction] = field( + default_factory=list, + metadata={ + "name": "Traction", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class FiniteElements: + class Meta: + name = "FiniteElementsType" + + finite_element_space: List[FiniteElementSpace] = field( + default_factory=list, + metadata={ + "name": "FiniteElementSpace", + "type": "Element", + "namespace": "", + }, + ) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class FiniteVolume: + class Meta: + name = "FiniteVolumeType" + + hybrid_mimetic_discretization: List[HybridMimeticDiscretization] = field( + default_factory=list, + metadata={ + "name": "HybridMimeticDiscretization", + "type": "Element", + "namespace": "", + }, + ) + two_point_flux_approximation: List[TwoPointFluxApproximation] = field( + default_factory=list, + metadata={ + "name": "TwoPointFluxApproximation", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class FlowProppantTransport: + class Meta: + name = "FlowProppantTransportType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + proppant_solver_name: str = field( + metadata={ + "name": "proppantSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Functions: + class Meta: + name = "FunctionsType" + + composite_function: List[CompositeFunction] = field( + default_factory=list, + metadata={ + "name": "CompositeFunction", + "type": "Element", + "namespace": "", + }, + ) + multivariable_table_function: List[MultivariableTableFunction] = field( + default_factory=list, + metadata={ + "name": "MultivariableTableFunction", + "type": "Element", + "namespace": "", + }, + ) + symbolic_function: List[SymbolicFunction] = field( + default_factory=list, + metadata={ + "name": "SymbolicFunction", + "type": "Element", + "namespace": "", + }, + ) + table_function: List[TableFunction] = field( + default_factory=list, + metadata={ + "name": "TableFunction", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Geometry: + class Meta: + name = "GeometryType" + + box: List[Box] = field( + default_factory=list, + metadata={ + "name": "Box", + "type": "Element", + "namespace": "", + }, + ) + custom_polar_object: List[CustomPolarObject] = field( + default_factory=list, + metadata={ + "name": "CustomPolarObject", + "type": "Element", + "namespace": "", + }, + ) + cylinder: List[Cylinder] = field( + default_factory=list, + metadata={ + "name": "Cylinder", + "type": "Element", + "namespace": "", + }, + ) + disc: List[Disc] = field( + default_factory=list, + metadata={ + "name": "Disc", + "type": "Element", + "namespace": "", + }, + ) + rectangle: List[Rectangle] = field( + default_factory=list, + metadata={ + "name": "Rectangle", + "type": "Element", + "namespace": "", + }, + ) + thick_plane: List[ThickPlane] = field( + default_factory=list, + metadata={ + "name": "ThickPlane", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Hydrofracture: + class Meta: + name = "HydrofractureType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_matrix_poroelastic: str = field( + default="0", + metadata={ + "name": "isMatrixPoroelastic", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + surface_generator_name: str = field( + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + use_quasi_newton: str = field( + default="0", + metadata={ + "name": "useQuasiNewton", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Included: + class Meta: + name = "IncludedType" + + file: List[File] = field( + default_factory=list, + metadata={ + "name": "File", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class InternalWell: + class Meta: + name = "InternalWellType" + + perforation: List[Perforation] = field( + default_factory=list, + metadata={ + "name": "Perforation", + "type": "Element", + "namespace": "", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + min_element_length: str = field( + default="0.001", + metadata={ + "name": "minElementLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_segment_length: str = field( + default="0.01", + metadata={ + "name": "minSegmentLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_elements_per_segment: str = field( + metadata={ + "name": "numElementsPerSegment", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + polyline_node_coords: str = field( + metadata={ + "name": "polylineNodeCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + } + ) + polyline_segment_conn: str = field( + metadata={ + "name": "polylineSegmentConn", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*\}\s*", + } + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + well_controls_name: str = field( + metadata={ + "name": "wellControlsName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + well_region_name: str = field( + metadata={ + "name": "wellRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class LaplaceFem: + class Meta: + name = "LaplaceFEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + field_name: str = field( + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|SteadyState|ImplicitTransient", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class MultiphasePoromechanicsReservoir: + class Meta: + name = "MultiphasePoromechanicsReservoirType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class MultiphasePoromechanics: + class Meta: + name = "MultiphasePoromechanicsType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + stabilization_multiplier: str = field( + default="1", + metadata={ + "name": "stabilizationMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_region_names: str = field( + default="{}", + metadata={ + "name": "stabilizationRegionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + stabilization_type: str = field( + default="None", + metadata={ + "name": "stabilizationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Global|Local", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Outputs: + class Meta: + name = "OutputsType" + + blueprint: List[Blueprint] = field( + default_factory=list, + metadata={ + "name": "Blueprint", + "type": "Element", + "namespace": "", + }, + ) + chombo_io: List[ChomboIo] = field( + default_factory=list, + metadata={ + "name": "ChomboIO", + "type": "Element", + "namespace": "", + }, + ) + python: List[Python] = field( + default_factory=list, + metadata={ + "name": "Python", + "type": "Element", + "namespace": "", + }, + ) + restart: List[Restart] = field( + default_factory=list, + metadata={ + "name": "Restart", + "type": "Element", + "namespace": "", + }, + ) + silo: List[Silo] = field( + default_factory=list, + metadata={ + "name": "Silo", + "type": "Element", + "namespace": "", + }, + ) + time_history: List[TimeHistory] = field( + default_factory=list, + metadata={ + "name": "TimeHistory", + "type": "Element", + "namespace": "", + }, + ) + vtk: List[Vtk] = field( + default_factory=list, + metadata={ + "name": "VTK", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Parameters: + class Meta: + name = "ParametersType" + + parameter: List[Parameter] = field( + default_factory=list, + metadata={ + "name": "Parameter", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class ParticleRegions: + class Meta: + name = "ParticleRegionsType" + + particle_region: List[ParticleRegion] = field( + default_factory=list, + metadata={ + "name": "ParticleRegion", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class PeriodicEvent: + class Meta: + name = "PeriodicEventType" + + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List[PeriodicEvent] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List[SoloEvent] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cycle_frequency: str = field( + default="1", + metadata={ + "name": "cycleFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + object_value: Optional[str] = field( + default=None, + metadata={ + "name": "object", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + set: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + stat: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_timestep: str = field( + default="1", + metadata={ + "name": "targetExactTimestep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + threshold: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_frequency: str = field( + default="-1", + metadata={ + "name": "timeFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PhaseFieldDamageFem: + class Meta: + name = "PhaseFieldDamageFEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + damage_upper_bound: str = field( + default="1.5", + metadata={ + "name": "damageUpperBound", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + field_name: str = field( + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + irreversibility_flag: str = field( + default="0", + metadata={ + "name": "irreversibilityFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + local_dissipation: str = field( + metadata={ + "name": "localDissipation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|Linear|Quadratic", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|SteadyState|ImplicitTransient|ExplicitTransient", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class PhaseFieldFracture: + class Meta: + name = "PhaseFieldFractureType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + damage_solver_name: str = field( + metadata={ + "name": "damageSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ProppantTransport: + class Meta: + name = "ProppantTransportType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + bridging_factor: str = field( + default="0", + metadata={ + "name": "bridgingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_shields_number: str = field( + default="0", + metadata={ + "name": "criticalShieldsNumber", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + friction_coefficient: str = field( + default="0.03", + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_density: str = field( + default="2500", + metadata={ + "name": "proppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: str = field( + default="0.0004", + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + update_proppant_packing: str = field( + default="0", + metadata={ + "name": "updateProppantPacking", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class ReactiveCompositionalMultiphaseObl: + class Meta: + name = "ReactiveCompositionalMultiphaseOBLType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + obloperators_table_file: str = field( + metadata={ + "name": "OBLOperatorsTableFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + } + ) + allow_local_oblchopping: str = field( + default="1", + metadata={ + "name": "allowLocalOBLChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + enable_energy_balance: str = field( + metadata={ + "name": "enableEnergyBalance", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="1", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_components: str = field( + metadata={ + "name": "numComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + num_phases: str = field( + metadata={ + "name": "numPhases", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + trans_mult_exp: str = field( + default="1", + metadata={ + "name": "transMultExp", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_dartsl2_norm: str = field( + default="1", + metadata={ + "name": "useDARTSL2Norm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseFvm: + class Meta: + name = "SinglePhaseFVMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseHybridFvm: + class Meta: + name = "SinglePhaseHybridFVMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhasePoromechanicsConformingFractures: + class Meta: + name = "SinglePhasePoromechanicsConformingFracturesType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhasePoromechanicsEmbeddedFractures: + class Meta: + name = "SinglePhasePoromechanicsEmbeddedFracturesType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhasePoromechanicsReservoir: + class Meta: + name = "SinglePhasePoromechanicsReservoirType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhasePoromechanics: + class Meta: + name = "SinglePhasePoromechanicsType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseProppantFvm: + class Meta: + name = "SinglePhaseProppantFVMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseReservoirPoromechanics: + class Meta: + name = "SinglePhaseReservoirPoromechanicsType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reservoir_and_wells_solver_name: str = field( + metadata={ + "name": "reservoirAndWellsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseReservoir: + class Meta: + name = "SinglePhaseReservoirType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SinglePhaseWell: + class Meta: + name = "SinglePhaseWellType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + well_controls: List[WellControls] = field( + default_factory=list, + metadata={ + "name": "WellControls", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsEmbeddedFractures: + class Meta: + name = "SolidMechanicsEmbeddedFracturesType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + use_static_condensation: str = field( + default="0", + metadata={ + "name": "useStaticCondensation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsLagrangeContact: + class Meta: + name = "SolidMechanicsLagrangeContactType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_name: str = field( + metadata={ + "name": "stabilizationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsLagrangianSsle: + class Meta: + name = "SolidMechanicsLagrangianSSLEType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + default="NOCONTACT", + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsLagrangianFem: + class Meta: + name = "SolidMechanics_LagrangianFEMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + default="NOCONTACT", + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SolidMechanicsMpm: + class Meta: + name = "SolidMechanics_MPMType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + boundary_condition_types: str = field( + default="{0}", + metadata={ + "name": "boundaryConditionTypes", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + box_average_history: str = field( + default="0", + metadata={ + "name": "boxAverageHistory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_gap_correction: str = field( + default="0", + metadata={ + "name": "contactGapCorrection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cpdi_domain_scaling: str = field( + default="0", + metadata={ + "name": "cpdiDomainScaling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + damage_field_partitioning: str = field( + default="0", + metadata={ + "name": "damageFieldPartitioning", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + f_table_interp_type: str = field( + default="0", + metadata={ + "name": "fTableInterpType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + f_table_path: Optional[str] = field( + default=None, + metadata={ + "name": "fTablePath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + friction_coefficient: str = field( + default="0", + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + needs_neighbor_list: str = field( + default="0", + metadata={ + "name": "needsNeighborList", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + neighbor_radius: str = field( + default="-1", + metadata={ + "name": "neighborRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + plane_strain: str = field( + default="0", + metadata={ + "name": "planeStrain", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + prescribed_bc_table: str = field( + default="0", + metadata={ + "name": "prescribedBcTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + prescribed_boundary_ftable: str = field( + default="0", + metadata={ + "name": "prescribedBoundaryFTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reaction_history: str = field( + default="0", + metadata={ + "name": "reactionHistory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + separability_min_damage: str = field( + default="0.5", + metadata={ + "name": "separabilityMinDamage", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + solver_profiling: str = field( + default="0", + metadata={ + "name": "solverProfiling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_detection: str = field( + default="0", + metadata={ + "name": "surfaceDetection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + treat_fully_damaged_as_single_field: str = field( + default="1", + metadata={ + "name": "treatFullyDamagedAsSingleField", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_damage_as_surface_flag: str = field( + default="0", + metadata={ + "name": "useDamageAsSurfaceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class SurfaceGenerator: + class Meta: + name = "SurfaceGeneratorType" + + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + fracture_region: str = field( + default="Fracture", + metadata={ + "name": "fractureRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_poroelastic: str = field( + default="0", + metadata={ + "name": "isPoroelastic", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mpi_comm_order: str = field( + default="0", + metadata={ + "name": "mpiCommOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + node_based_sif: str = field( + default="0", + metadata={ + "name": "nodeBasedSIF", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + rock_toughness: str = field( + metadata={ + "name": "rockToughness", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Tasks: + class Meta: + name = "TasksType" + + compositional_multiphase_reservoir_poromechanics_initialization: List[ + CompositionalMultiphaseReservoirPoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoirPoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_statistics: List[CompositionalMultiphaseStatistics] = ( + field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseStatistics", + "type": "Element", + "namespace": "", + }, + ) + ) + multiphase_poromechanics_initialization: List[ + MultiphasePoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + pvtdriver: List[Pvtdriver] = field( + default_factory=list, + metadata={ + "name": "PVTDriver", + "type": "Element", + "namespace": "", + }, + ) + pack_collection: List[PackCollection] = field( + default_factory=list, + metadata={ + "name": "PackCollection", + "type": "Element", + "namespace": "", + }, + ) + reactive_fluid_driver: List[ReactiveFluidDriver] = field( + default_factory=list, + metadata={ + "name": "ReactiveFluidDriver", + "type": "Element", + "namespace": "", + }, + ) + relperm_driver: List[RelpermDriver] = field( + default_factory=list, + metadata={ + "name": "RelpermDriver", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_initialization: List[ + SinglePhasePoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir_poromechanics_initialization: List[ + SinglePhaseReservoirPoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoirPoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + single_phase_statistics: List[SinglePhaseStatistics] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseStatistics", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_state_reset: List[SolidMechanicsStateReset] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsStateReset", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_statistics: List[SolidMechanicsStatistics] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsStatistics", + "type": "Element", + "namespace": "", + }, + ) + triaxial_driver: List[TriaxialDriver] = field( + default_factory=list, + metadata={ + "name": "TriaxialDriver", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Vtkwell: + class Meta: + name = "VTKWellType" + + perforation: List[Perforation] = field( + default_factory=list, + metadata={ + "name": "Perforation", + "type": "Element", + "namespace": "", + }, + ) + file: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + } + ) + min_element_length: str = field( + default="0.001", + metadata={ + "name": "minElementLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_segment_length: str = field( + default="0.01", + metadata={ + "name": "minSegmentLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_elements_per_segment: str = field( + metadata={ + "name": "numElementsPerSegment", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + well_controls_name: str = field( + metadata={ + "name": "wellControlsName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + well_region_name: str = field( + metadata={ + "name": "wellRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Crusher: + class Meta: + name = "crusherType" + + run: List[Run] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Lassen: + class Meta: + name = "lassenType" + + run: List[Run] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Quartz: + class Meta: + name = "quartzType" + + run: List[Run] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Benchmarks: + class Meta: + name = "BenchmarksType" + + crusher: List[Crusher] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + lassen: List[Lassen] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + quartz: List[Quartz] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class InternalMesh: + class Meta: + name = "InternalMeshType" + + internal_well: List[InternalWell] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + vtkwell: List[Vtkwell] = field( + default_factory=list, + metadata={ + "name": "VTKWell", + "type": "Element", + "namespace": "", + }, + ) + cell_block_names: str = field( + metadata={ + "name": "cellBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + element_types: str = field( + metadata={ + "name": "elementTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + nx: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + ny: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + nz: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + position_tolerance: str = field( + default="1e-10", + metadata={ + "name": "positionTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + triangle_pattern: str = field( + default="0", + metadata={ + "name": "trianglePattern", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + x_bias: str = field( + default="{1}", + metadata={ + "name": "xBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + x_coords: str = field( + metadata={ + "name": "xCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + y_bias: str = field( + default="{1}", + metadata={ + "name": "yBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_coords: str = field( + metadata={ + "name": "yCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + z_bias: str = field( + default="{1}", + metadata={ + "name": "zBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_coords: str = field( + metadata={ + "name": "zCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class InternalWellbore: + class Meta: + name = "InternalWellboreType" + + internal_well: List[InternalWell] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + vtkwell: List[Vtkwell] = field( + default_factory=list, + metadata={ + "name": "VTKWell", + "type": "Element", + "namespace": "", + }, + ) + auto_space_radial_elems: str = field( + default="{-1}", + metadata={ + "name": "autoSpaceRadialElems", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + cartesian_mapping_inner_radius: str = field( + default="1e+99", + metadata={ + "name": "cartesianMappingInnerRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cell_block_names: str = field( + metadata={ + "name": "cellBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + element_types: str = field( + metadata={ + "name": "elementTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + hard_radial_coords: str = field( + default="{0}", + metadata={ + "name": "hardRadialCoords", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + nr: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + nt: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + nz: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + position_tolerance: str = field( + default="1e-10", + metadata={ + "name": "positionTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + r_bias: str = field( + default="{-0.8}", + metadata={ + "name": "rBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + theta: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + trajectory: str = field( + default="{{0}}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + triangle_pattern: str = field( + default="0", + metadata={ + "name": "trianglePattern", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_cartesian_outer_boundary: str = field( + default="1000000", + metadata={ + "name": "useCartesianOuterBoundary", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + x_bias: str = field( + default="{1}", + metadata={ + "name": "xBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_bias: str = field( + default="{1}", + metadata={ + "name": "yBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_bias: str = field( + default="{1}", + metadata={ + "name": "zBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_coords: str = field( + metadata={ + "name": "zCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class NumericalMethods: + class Meta: + name = "NumericalMethodsType" + + finite_elements: List[FiniteElements] = field( + default_factory=list, + metadata={ + "name": "FiniteElements", + "type": "Element", + "namespace": "", + }, + ) + finite_volume: List[FiniteVolume] = field( + default_factory=list, + metadata={ + "name": "FiniteVolume", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class SoloEvent: + class Meta: + name = "SoloEventType" + + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List[PeriodicEvent] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List[SoloEvent] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_cycle: str = field( + default="-1", + metadata={ + "name": "targetCycle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_timestep: str = field( + default="1", + metadata={ + "name": "targetExactTimestep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_time: str = field( + default="-1", + metadata={ + "name": "targetTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Solvers: + class Meta: + name = "SolversType" + + acoustic_elastic_sem: List[AcousticElasticSem] = field( + default_factory=list, + metadata={ + "name": "AcousticElasticSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_first_order_sem: List[AcousticFirstOrderSem] = field( + default_factory=list, + metadata={ + "name": "AcousticFirstOrderSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_sem: List[AcousticSem] = field( + default_factory=list, + metadata={ + "name": "AcousticSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_vtisem: List[AcousticVtisem] = field( + default_factory=list, + metadata={ + "name": "AcousticVTISEM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_fvm: List[CompositionalMultiphaseFvm] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseFVM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_hybrid_fvm: List[CompositionalMultiphaseHybridFvm] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseHybridFVM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_reservoir: List[CompositionalMultiphaseReservoir] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoir", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_reservoir_poromechanics: List[ + CompositionalMultiphaseReservoirPoromechanics + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoirPoromechanics", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_well: List[CompositionalMultiphaseWell] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseWell", + "type": "Element", + "namespace": "", + }, + ) + elastic_first_order_sem: List[ElasticFirstOrderSem] = field( + default_factory=list, + metadata={ + "name": "ElasticFirstOrderSEM", + "type": "Element", + "namespace": "", + }, + ) + elastic_sem: List[ElasticSem] = field( + default_factory=list, + metadata={ + "name": "ElasticSEM", + "type": "Element", + "namespace": "", + }, + ) + embedded_surface_generator: List[EmbeddedSurfaceGenerator] = field( + default_factory=list, + metadata={ + "name": "EmbeddedSurfaceGenerator", + "type": "Element", + "namespace": "", + }, + ) + flow_proppant_transport: List[FlowProppantTransport] = field( + default_factory=list, + metadata={ + "name": "FlowProppantTransport", + "type": "Element", + "namespace": "", + }, + ) + hydrofracture: List[Hydrofracture] = field( + default_factory=list, + metadata={ + "name": "Hydrofracture", + "type": "Element", + "namespace": "", + }, + ) + laplace_fem: List[LaplaceFem] = field( + default_factory=list, + metadata={ + "name": "LaplaceFEM", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics: List[MultiphasePoromechanics] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanics", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics_reservoir: List[MultiphasePoromechanicsReservoir] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanicsReservoir", + "type": "Element", + "namespace": "", + }, + ) + phase_field_damage_fem: List[PhaseFieldDamageFem] = field( + default_factory=list, + metadata={ + "name": "PhaseFieldDamageFEM", + "type": "Element", + "namespace": "", + }, + ) + phase_field_fracture: List[PhaseFieldFracture] = field( + default_factory=list, + metadata={ + "name": "PhaseFieldFracture", + "type": "Element", + "namespace": "", + }, + ) + proppant_transport: List[ProppantTransport] = field( + default_factory=list, + metadata={ + "name": "ProppantTransport", + "type": "Element", + "namespace": "", + }, + ) + reactive_compositional_multiphase_obl: List[ReactiveCompositionalMultiphaseObl] = ( + field( + default_factory=list, + metadata={ + "name": "ReactiveCompositionalMultiphaseOBL", + "type": "Element", + "namespace": "", + }, + ) + ) + single_phase_fvm: List[SinglePhaseFvm] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_hybrid_fvm: List[SinglePhaseHybridFvm] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseHybridFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics: List[SinglePhasePoromechanics] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanics", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_conforming_fractures: List[ + SinglePhasePoromechanicsConformingFractures + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsConformingFractures", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_embedded_fractures: List[ + SinglePhasePoromechanicsEmbeddedFractures + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsEmbeddedFractures", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_reservoir: List[SinglePhasePoromechanicsReservoir] = ( + field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsReservoir", + "type": "Element", + "namespace": "", + }, + ) + ) + single_phase_proppant_fvm: List[SinglePhaseProppantFvm] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseProppantFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir: List[SinglePhaseReservoir] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoir", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir_poromechanics: List[SinglePhaseReservoirPoromechanics] = ( + field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoirPoromechanics", + "type": "Element", + "namespace": "", + }, + ) + ) + single_phase_well: List[SinglePhaseWell] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseWell", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_embedded_fractures: List[SolidMechanicsEmbeddedFractures] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsEmbeddedFractures", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrange_contact: List[SolidMechanicsLagrangeContact] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsLagrangeContact", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrangian_ssle: List[SolidMechanicsLagrangianSsle] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsLagrangianSSLE", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrangian_fem: List[SolidMechanicsLagrangianFem] = field( + default_factory=list, + metadata={ + "name": "SolidMechanics_LagrangianFEM", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_mpm: List[SolidMechanicsMpm] = field( + default_factory=list, + metadata={ + "name": "SolidMechanics_MPM", + "type": "Element", + "namespace": "", + }, + ) + surface_generator: List[SurfaceGenerator] = field( + default_factory=list, + metadata={ + "name": "SurfaceGenerator", + "type": "Element", + "namespace": "", + }, + ) + gravity_vector: str = field( + default="{0,0,-9.81}", + metadata={ + "name": "gravityVector", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + + +@dataclass(kw_only=True) +class Vtkmesh: + class Meta: + name = "VTKMeshType" + + internal_well: List[InternalWell] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + vtkwell: List[Vtkwell] = field( + default_factory=list, + metadata={ + "name": "VTKWell", + "type": "Element", + "namespace": "", + }, + ) + face_blocks: str = field( + default="{}", + metadata={ + "name": "faceBlocks", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + field_names_in_geosx: str = field( + default="{}", + metadata={ + "name": "fieldNamesInGEOSX", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + fields_to_import: str = field( + default="{}", + metadata={ + "name": "fieldsToImport", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + file: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + main_block_name: str = field( + default="main", + metadata={ + "name": "mainBlockName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + nodeset_names: str = field( + default="{}", + metadata={ + "name": "nodesetNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + partition_method: str = field( + default="parmetis", + metadata={ + "name": "partitionMethod", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|parmetis|ptscotch", + }, + ) + partition_refinement: str = field( + default="1", + metadata={ + "name": "partitionRefinement", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + region_attribute: str = field( + default="attribute", + metadata={ + "name": "regionAttribute", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="{1,1,1}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + surfacic_fields_in_geosx: str = field( + default="{}", + metadata={ + "name": "surfacicFieldsInGEOSX", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + surfacic_fields_to_import: str = field( + default="{}", + metadata={ + "name": "surfacicFieldsToImport", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + translate: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + use_global_ids: str = field( + default="0", + metadata={ + "name": "useGlobalIds", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +@dataclass(kw_only=True) +class Events: + class Meta: + name = "EventsType" + + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List[PeriodicEvent] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List[SoloEvent] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_cycle: str = field( + default="2147483647", + metadata={ + "name": "maxCycle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_time: str = field( + default="1.79769e+308", + metadata={ + "name": "maxTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_time: str = field( + default="0", + metadata={ + "name": "minTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_output_format: str = field( + default="seconds", + metadata={ + "name": "timeOutputFormat", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|seconds|minutes|hours|days|years|full", + }, + ) + + +@dataclass(kw_only=True) +class Mesh: + class Meta: + name = "MeshType" + + internal_mesh: List[InternalMesh] = field( + default_factory=list, + metadata={ + "name": "InternalMesh", + "type": "Element", + "namespace": "", + }, + ) + internal_wellbore: List[InternalWellbore] = field( + default_factory=list, + metadata={ + "name": "InternalWellbore", + "type": "Element", + "namespace": "", + }, + ) + particle_mesh: List[ParticleMesh] = field( + default_factory=list, + metadata={ + "name": "ParticleMesh", + "type": "Element", + "namespace": "", + }, + ) + vtkmesh: List[Vtkmesh] = field( + default_factory=list, + metadata={ + "name": "VTKMesh", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass(kw_only=True) +class Problem: + class Meta: + name = "ProblemType" + + events: List[Events] = field( + default_factory=list, + metadata={ + "name": "Events", + "type": "Element", + "namespace": "", + }, + ) + field_specifications: List[FieldSpecifications] = field( + default_factory=list, + metadata={ + "name": "FieldSpecifications", + "type": "Element", + "namespace": "", + }, + ) + functions: List[Functions] = field( + default_factory=list, + metadata={ + "name": "Functions", + "type": "Element", + "namespace": "", + }, + ) + geometry: List[Geometry] = field( + default_factory=list, + metadata={ + "name": "Geometry", + "type": "Element", + "namespace": "", + }, + ) + mesh: List[Mesh] = field( + default_factory=list, + metadata={ + "name": "Mesh", + "type": "Element", + "namespace": "", + }, + ) + numerical_methods: List[NumericalMethods] = field( + default_factory=list, + metadata={ + "name": "NumericalMethods", + "type": "Element", + "namespace": "", + }, + ) + outputs: List[Outputs] = field( + default_factory=list, + metadata={ + "name": "Outputs", + "type": "Element", + "namespace": "", + }, + ) + solvers: List[Solvers] = field( + default_factory=list, + metadata={ + "name": "Solvers", + "type": "Element", + "namespace": "", + }, + ) + tasks: List[Tasks] = field( + default_factory=list, + metadata={ + "name": "Tasks", + "type": "Element", + "namespace": "", + }, + ) + constitutive: List[Constitutive] = field( + default_factory=list, + metadata={ + "name": "Constitutive", + "type": "Element", + "namespace": "", + }, + ) + element_regions: List[ElementRegions] = field( + default_factory=list, + metadata={ + "name": "ElementRegions", + "type": "Element", + "namespace": "", + }, + ) + particle_regions: List[ParticleRegions] = field( + default_factory=list, + metadata={ + "name": "ParticleRegions", + "type": "Element", + "namespace": "", + }, + ) + included: List[Included] = field( + default_factory=list, + metadata={ + "name": "Included", + "type": "Element", + "namespace": "", + }, + ) + parameters: List[Parameters] = field( + default_factory=list, + metadata={ + "name": "Parameters", + "type": "Element", + "namespace": "", + }, + ) + benchmarks: List[Benchmarks] = field( + default_factory=list, + metadata={ + "name": "Benchmarks", + "type": "Element", + "namespace": "", + }, + ) diff --git a/geos-trame/src/geos_trame/schema_generated/schema_mod.py b/geos-trame/src/geos_trame/schema_generated/schema_mod.py new file mode 100644 index 00000000..f33f5a82 --- /dev/null +++ b/geos-trame/src/geos_trame/schema_generated/schema_mod.py @@ -0,0 +1,16568 @@ +"""This file was generated by xsdata, v24.6.1, on 2024-07-09 14:43:42 + +Generator: PydanticGenerator +See: https://xsdata.readthedocs.io/ +""" + +from typing import List, Optional + +from pydantic import BaseModel, ConfigDict +from xsdata_pydantic.fields import field + + +class Aquifer(BaseModel): + class Meta: + name = "Aquifer" + + model_config = ConfigDict(defer_build=True) + allow_all_phases_into_aquifer: str = field( + default="0", + metadata={ + "name": "allowAllPhasesIntoAquifer", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + aquifer_angle: str = field( + metadata={ + "name": "aquiferAngle", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_elevation: str = field( + metadata={ + "name": "aquiferElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_initial_pressure: str = field( + metadata={ + "name": "aquiferInitialPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_inner_radius: str = field( + metadata={ + "name": "aquiferInnerRadius", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_permeability: str = field( + metadata={ + "name": "aquiferPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_porosity: str = field( + metadata={ + "name": "aquiferPorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_thickness: str = field( + metadata={ + "name": "aquiferThickness", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_total_compressibility: str = field( + metadata={ + "name": "aquiferTotalCompressibility", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_water_density: str = field( + metadata={ + "name": "aquiferWaterDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + aquifer_water_phase_component_fraction: str = field( + default="{0}", + metadata={ + "name": "aquiferWaterPhaseComponentFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + aquifer_water_phase_component_names: str = field( + default="{}", + metadata={ + "name": "aquiferWaterPhaseComponentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + aquifer_water_viscosity: str = field( + metadata={ + "name": "aquiferWaterViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + pressure_influence_function_name: Optional[str] = field( + default=None, + metadata={ + "name": "pressureInfluenceFunctionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class BiotPorosity(BaseModel): + class Meta: + name = "BiotPorosity" + + model_config = ConfigDict(defer_build=True) + default_porosity_tec: str = field( + default="0", + metadata={ + "name": "defaultPorosityTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_reference_porosity: str = field( + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + grain_bulk_modulus: str = field( + metadata={ + "name": "grainBulkModulus", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + use_uniaxial_fixed_stress: str = field( + default="0", + metadata={ + "name": "useUniaxialFixedStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class BlackOilFluid(BaseModel): + class Meta: + name = "BlackOilFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hydrocarbon_formation_vol_factor_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonFormationVolFactorTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + hydrocarbon_viscosity_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonViscosityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + surface_densities: str = field( + metadata={ + "name": "surfaceDensities", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + table_files: str = field( + default="{}", + metadata={ + "name": "tableFiles", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + }, + ) + water_compressibility: str = field( + default="0", + metadata={ + "name": "waterCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_formation_volume_factor: str = field( + default="0", + metadata={ + "name": "waterFormationVolumeFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_reference_pressure: str = field( + default="0", + metadata={ + "name": "waterReferencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_viscosity: str = field( + default="0", + metadata={ + "name": "waterViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Blueprint(BaseModel): + class Meta: + name = "Blueprint" + + model_config = ConfigDict(defer_build=True) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_full_quadrature_data: str = field( + default="0", + metadata={ + "name": "outputFullQuadratureData", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Box(BaseModel): + class Meta: + name = "Box" + + model_config = ConfigDict(defer_build=True) + strike: str = field( + default="-90", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + x_max: str = field( + metadata={ + "name": "xMax", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + x_min: str = field( + metadata={ + "name": "xMin", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class BrooksCoreyBakerRelativePermeability(BaseModel): + class Meta: + name = "BrooksCoreyBakerRelativePermeability" + + model_config = ConfigDict(defer_build=True) + gas_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "gasOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "waterOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class BrooksCoreyCapillaryPressure(BaseModel): + class Meta: + name = "BrooksCoreyCapillaryPressure" + + model_config = ConfigDict(defer_build=True) + cap_pressure_epsilon: str = field( + default="1e-06", + metadata={ + "name": "capPressureEpsilon", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_cap_pressure_exponent_inv: str = field( + default="{2}", + metadata={ + "name": "phaseCapPressureExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_entry_pressure: str = field( + default="{1}", + metadata={ + "name": "phaseEntryPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class BrooksCoreyRelativePermeability(BaseModel): + class Meta: + name = "BrooksCoreyRelativePermeability" + + model_config = ConfigDict(defer_build=True) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + phase_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "phaseRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "phaseRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class BrooksCoreyStone2RelativePermeability(BaseModel): + class Meta: + name = "BrooksCoreyStone2RelativePermeability" + + model_config = ConfigDict(defer_build=True) + gas_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "gasOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "waterOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Co2BrineEzrokhiFluid(BaseModel): + class Meta: + name = "CO2BrineEzrokhiFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Co2BrineEzrokhiThermalFluid(BaseModel): + class Meta: + name = "CO2BrineEzrokhiThermalFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Co2BrinePhillipsFluid(BaseModel): + class Meta: + name = "CO2BrinePhillipsFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Co2BrinePhillipsThermalFluid(BaseModel): + class Meta: + name = "CO2BrinePhillipsThermalFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + } + ) + solubility_table_names: str = field( + default="{}", + metadata={ + "name": "solubilityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CarmanKozenyPermeability(BaseModel): + class Meta: + name = "CarmanKozenyPermeability" + + model_config = ConfigDict(defer_build=True) + anisotropy: str = field( + default="{1,1,1}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + particle_diameter: str = field( + metadata={ + "name": "particleDiameter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + sphericity: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CellElementRegion(BaseModel): + class Meta: + name = "CellElementRegion" + + model_config = ConfigDict(defer_build=True) + cell_blocks: str = field( + metadata={ + "name": "cellBlocks", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + coarsening_ratio: str = field( + default="0", + metadata={ + "name": "coarseningRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CeramicDamage(BaseModel): + class Meta: + name = "CeramicDamage" + + model_config = ConfigDict(defer_build=True) + compressive_strength: str = field( + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + crack_speed: str = field( + metadata={ + "name": "crackSpeed", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + maximum_strength: str = field( + metadata={ + "name": "maximumStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ChomboIo(BaseModel): + class Meta: + name = "ChomboIO" + + model_config = ConfigDict(defer_build=True) + begin_cycle: str = field( + metadata={ + "name": "beginCycle", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + input_path: str = field( + default="/INVALID_INPUT_PATH", + metadata={ + "name": "inputPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_path: str = field( + metadata={ + "name": "outputPath", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_chombo_pressures: str = field( + default="0", + metadata={ + "name": "useChomboPressures", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + wait_for_input: str = field( + metadata={ + "name": "waitForInput", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositeFunction(BaseModel): + class Meta: + name = "CompositeFunction" + + model_config = ConfigDict(defer_build=True) + expression: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + function_names: str = field( + default="{}", + metadata={ + "name": "functionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + variable_names: str = field( + default="{}", + metadata={ + "name": "variableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseFluid(BaseModel): + class Meta: + name = "CompositionalMultiphaseFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: str = field( + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: str = field( + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_temperature: str = field( + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + equations_of_state: str = field( + metadata={ + "name": "equationsOfState", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseReservoirPoromechanicsInitialization(BaseModel): + class Meta: + name = "CompositionalMultiphaseReservoirPoromechanicsInitialization" + + model_config = ConfigDict(defer_build=True) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseStatistics(BaseModel): + class Meta: + name = "CompositionalMultiphaseStatistics" + + model_config = ConfigDict(defer_build=True) + compute_cflnumbers: str = field( + default="0", + metadata={ + "name": "computeCFLNumbers", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + compute_region_statistics: str = field( + default="1", + metadata={ + "name": "computeRegionStatistics", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + relperm_threshold: str = field( + default="1e-06", + metadata={ + "name": "relpermThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositonalTwoPhaseFluidPengRobinson(BaseModel): + class Meta: + name = "CompositonalTwoPhaseFluidPengRobinson" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: str = field( + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: str = field( + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_temperature: str = field( + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_volume: str = field( + default="{0}", + metadata={ + "name": "componentCriticalVolume", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositonalTwoPhaseFluidSoaveRedlichKwong(BaseModel): + class Meta: + name = "CompositonalTwoPhaseFluidSoaveRedlichKwong" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: str = field( + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: str = field( + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_temperature: str = field( + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_critical_volume: str = field( + default="{0}", + metadata={ + "name": "componentCriticalVolume", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSinglePhaseFluid(BaseModel): + class Meta: + name = "CompressibleSinglePhaseFluid" + + model_config = ConfigDict(defer_build=True) + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_viscosity: str = field( + metadata={ + "name": "defaultViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + density_model_type: str = field( + default="linear", + metadata={ + "name": "densityModel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="0", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosity_model_type: str = field( + default="linear", + metadata={ + "name": "viscosityModel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSolidCarmanKozenyPermeability(BaseModel): + class Meta: + name = "CompressibleSolidCarmanKozenyPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSolidConstantPermeability(BaseModel): + class Meta: + name = "CompressibleSolidConstantPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSolidExponentialDecayPermeability(BaseModel): + class Meta: + name = "CompressibleSolidExponentialDecayPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSolidParallelPlatesPermeability(BaseModel): + class Meta: + name = "CompressibleSolidParallelPlatesPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSolidSlipDependentPermeability(BaseModel): + class Meta: + name = "CompressibleSolidSlipDependentPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompressibleSolidWillisRichardsPermeability(BaseModel): + class Meta: + name = "CompressibleSolidWillisRichardsPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ConstantDiffusion(BaseModel): + class Meta: + name = "ConstantDiffusion" + + model_config = ConfigDict(defer_build=True) + default_phase_diffusivity_multipliers: str = field( + default="{1}", + metadata={ + "name": "defaultPhaseDiffusivityMultipliers", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + diffusivity_components: str = field( + metadata={ + "name": "diffusivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ConstantPermeability(BaseModel): + class Meta: + name = "ConstantPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_components: str = field( + metadata={ + "name": "permeabilityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Coulomb(BaseModel): + class Meta: + name = "Coulomb" + + model_config = ConfigDict(defer_build=True) + aperture_table_name: str = field( + metadata={ + "name": "apertureTableName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + aperture_tolerance: str = field( + default="1e-09", + metadata={ + "name": "apertureTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cohesion: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + displacement_jump_threshold: str = field( + default="2.22045e-16", + metadata={ + "name": "displacementJumpThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + friction_coefficient: str = field( + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + penalty_stiffness: str = field( + default="0", + metadata={ + "name": "penaltyStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_stiffness: str = field( + default="0", + metadata={ + "name": "shearStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CustomPolarObject(BaseModel): + class Meta: + name = "CustomPolarObject" + + model_config = ConfigDict(defer_build=True) + center: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + coefficients: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + length_vector: str = field( + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: str = field( + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Cylinder(BaseModel): + class Meta: + name = "Cylinder" + + model_config = ConfigDict(defer_build=True) + first_face_center: str = field( + metadata={ + "name": "firstFaceCenter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + inner_radius: str = field( + default="-1", + metadata={ + "name": "innerRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + outer_radius: str = field( + metadata={ + "name": "outerRadius", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + second_face_center: str = field( + metadata={ + "name": "secondFaceCenter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class DamageElasticIsotropic(BaseModel): + class Meta: + name = "DamageElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: str = field( + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + critical_strain_energy: str = field( + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: str = field( + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class DamageSpectralElasticIsotropic(BaseModel): + class Meta: + name = "DamageSpectralElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: str = field( + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + critical_strain_energy: str = field( + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: str = field( + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class DamageVolDevElasticIsotropic(BaseModel): + class Meta: + name = "DamageVolDevElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: str = field( + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + critical_strain_energy: str = field( + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: str = field( + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class DeadOilFluid(BaseModel): + class Meta: + name = "DeadOilFluid" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hydrocarbon_formation_vol_factor_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonFormationVolFactorTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + hydrocarbon_viscosity_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonViscosityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + surface_densities: str = field( + metadata={ + "name": "surfaceDensities", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + table_files: str = field( + default="{}", + metadata={ + "name": "tableFiles", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + }, + ) + water_compressibility: str = field( + default="0", + metadata={ + "name": "waterCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_formation_volume_factor: str = field( + default="0", + metadata={ + "name": "waterFormationVolumeFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_reference_pressure: str = field( + default="0", + metadata={ + "name": "waterReferencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_viscosity: str = field( + default="0", + metadata={ + "name": "waterViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class DelftEgg(BaseModel): + class Meta: + name = "DelftEgg" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shape_parameter: str = field( + default="1", + metadata={ + "name": "defaultShapeParameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Dirichlet(BaseModel): + class Meta: + name = "Dirichlet" + + model_config = ConfigDict(defer_build=True) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Disc(BaseModel): + class Meta: + name = "Disc" + + model_config = ConfigDict(defer_build=True) + center: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + length_vector: str = field( + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: str = field( + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class DruckerPrager(BaseModel): + class Meta: + name = "DruckerPrager" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_angle: str = field( + default="30", + metadata={ + "name": "defaultDilationAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening_rate: str = field( + default="0", + metadata={ + "name": "defaultHardeningRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ElasticIsotropicPressureDependent(BaseModel): + class Meta: + name = "ElasticIsotropicPressureDependent" + + model_config = ConfigDict(defer_build=True) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ElasticIsotropic(BaseModel): + class Meta: + name = "ElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ElasticOrthotropic(BaseModel): + class Meta: + name = "ElasticOrthotropic" + + model_config = ConfigDict(defer_build=True) + default_c11: str = field( + default="-1", + metadata={ + "name": "defaultC11", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c12: str = field( + default="-1", + metadata={ + "name": "defaultC12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c13: str = field( + default="-1", + metadata={ + "name": "defaultC13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c22: str = field( + default="-1", + metadata={ + "name": "defaultC22", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c23: str = field( + default="-1", + metadata={ + "name": "defaultC23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c33: str = field( + default="-1", + metadata={ + "name": "defaultC33", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c44: str = field( + default="-1", + metadata={ + "name": "defaultC44", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c55: str = field( + default="-1", + metadata={ + "name": "defaultC55", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c66: str = field( + default="-1", + metadata={ + "name": "defaultC66", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e1: str = field( + default="-1", + metadata={ + "name": "defaultE1", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e2: str = field( + default="-1", + metadata={ + "name": "defaultE2", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e3: str = field( + default="-1", + metadata={ + "name": "defaultE3", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g12: str = field( + default="-1", + metadata={ + "name": "defaultG12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g13: str = field( + default="-1", + metadata={ + "name": "defaultG13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g23: str = field( + default="-1", + metadata={ + "name": "defaultG23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu12: str = field( + default="-1", + metadata={ + "name": "defaultNu12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu13: str = field( + default="-1", + metadata={ + "name": "defaultNu13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu23: str = field( + default="-1", + metadata={ + "name": "defaultNu23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ElasticTransverseIsotropic(BaseModel): + class Meta: + name = "ElasticTransverseIsotropic" + + model_config = ConfigDict(defer_build=True) + default_c11: str = field( + default="-1", + metadata={ + "name": "defaultC11", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c13: str = field( + default="-1", + metadata={ + "name": "defaultC13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c33: str = field( + default="-1", + metadata={ + "name": "defaultC33", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c44: str = field( + default="-1", + metadata={ + "name": "defaultC44", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c66: str = field( + default="-1", + metadata={ + "name": "defaultC66", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio_axial_transverse: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatioAxialTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio_transverse: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatioTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus_axial_transverse: str = field( + default="-1", + metadata={ + "name": "defaultShearModulusAxialTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus_axial: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulusAxial", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus_transverse: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulusTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ExponentialDecayPermeability(BaseModel): + class Meta: + name = "ExponentialDecayPermeability" + + model_config = ConfigDict(defer_build=True) + empirical_constant: str = field( + metadata={ + "name": "empiricalConstant", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + initial_permeability: str = field( + metadata={ + "name": "initialPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ExtendedDruckerPrager(BaseModel): + class Meta: + name = "ExtendedDruckerPrager" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_ratio: str = field( + default="1", + metadata={ + "name": "defaultDilationRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening: str = field( + default="0", + metadata={ + "name": "defaultHardening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_initial_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultInitialFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_residual_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultResidualFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class FieldSpecification(BaseModel): + class Meta: + name = "FieldSpecification" + + model_config = ConfigDict(defer_build=True) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class File(BaseModel): + class Meta: + name = "File" + + model_config = ConfigDict(defer_build=True) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + } + ) + + +class FiniteElementSpace(BaseModel): + class Meta: + name = "FiniteElementSpace" + + model_config = ConfigDict(defer_build=True) + formulation: str = field( + default="default", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|SEM", + }, + ) + order: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + use_virtual_elements: str = field( + default="0", + metadata={ + "name": "useVirtualElements", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class FrictionlessContact(BaseModel): + class Meta: + name = "FrictionlessContact" + + model_config = ConfigDict(defer_build=True) + aperture_table_name: str = field( + metadata={ + "name": "apertureTableName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + aperture_tolerance: str = field( + default="1e-09", + metadata={ + "name": "apertureTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + displacement_jump_threshold: str = field( + default="2.22045e-16", + metadata={ + "name": "displacementJumpThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + penalty_stiffness: str = field( + default="0", + metadata={ + "name": "penaltyStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_stiffness: str = field( + default="0", + metadata={ + "name": "shearStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class HaltEvent(BaseModel): + class Meta: + name = "HaltEvent" + + model_config = ConfigDict(defer_build=True) + halt_event: List["HaltEvent"] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List["PeriodicEvent"] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List["SoloEvent"] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_runtime: str = field( + metadata={ + "name": "maxRuntime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class HybridMimeticDiscretization(BaseModel): + class Meta: + name = "HybridMimeticDiscretization" + + model_config = ConfigDict(defer_build=True) + inner_product_type: str = field( + metadata={ + "name": "innerProduct", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class HydrostaticEquilibrium(BaseModel): + class Meta: + name = "HydrostaticEquilibrium" + + model_config = ConfigDict(defer_build=True) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component_fraction_vs_elevation_table_names: str = field( + default="{}", + metadata={ + "name": "componentFractionVsElevationTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + datum_elevation: str = field( + metadata={ + "name": "datumElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + datum_pressure: str = field( + metadata={ + "name": "datumPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + elevation_increment_in_hydrostatic_pressure_table: str = field( + default="0.6096", + metadata={ + "name": "elevationIncrementInHydrostaticPressureTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + equilibration_tolerance: str = field( + default="0.001", + metadata={ + "name": "equilibrationTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_phase_name: Optional[str] = field( + default=None, + metadata={ + "name": "initialPhaseName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_number_of_equilibration_iterations: str = field( + default="5", + metadata={ + "name": "maxNumberOfEquilibrationIterations", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature_vs_elevation_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "temperatureVsElevationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class JfunctionCapillaryPressure(BaseModel): + class Meta: + name = "JFunctionCapillaryPressure" + + model_config = ConfigDict(defer_build=True) + non_wetting_intermediate_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "nonWettingIntermediateJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + non_wetting_intermediate_surface_tension: str = field( + default="0", + metadata={ + "name": "nonWettingIntermediateSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + permeability_direction: str = field( + metadata={ + "name": "permeabilityDirection", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|XY|X|Y|Z", + } + ) + permeability_exponent: str = field( + default="0.5", + metadata={ + "name": "permeabilityExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + porosity_exponent: str = field( + default="0.5", + metadata={ + "name": "porosityExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + wetting_intermediate_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingIntermediateJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_intermediate_surface_tension: str = field( + default="0", + metadata={ + "name": "wettingIntermediateSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + wetting_non_wetting_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingNonWettingJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_non_wetting_surface_tension: str = field( + default="0", + metadata={ + "name": "wettingNonWettingSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class LinearIsotropicDispersion(BaseModel): + class Meta: + name = "LinearIsotropicDispersion" + + model_config = ConfigDict(defer_build=True) + longitudinal_dispersivity: str = field( + metadata={ + "name": "longitudinalDispersivity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class LinearSolverParameters(BaseModel): + class Meta: + name = "LinearSolverParameters" + + model_config = ConfigDict(defer_build=True) + amg_aggressive_coarsening_levels: str = field( + default="0", + metadata={ + "name": "amgAggressiveCoarseningLevels", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_aggressive_coarsening_paths: str = field( + default="1", + metadata={ + "name": "amgAggressiveCoarseningPaths", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_aggressive_interp_type: str = field( + default="multipass", + metadata={ + "name": "amgAggressiveInterp", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|extendedIStage2|standardStage2|extendedStage2|multipass|modifiedExtended|modifiedExtendedI|modifiedExtendedE|modifiedMultipass", + }, + ) + amg_coarse_solver: str = field( + default="direct", + metadata={ + "name": "amgCoarseSolver", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|jacobi|l1jacobi|fgs|sgs|l1sgs|chebyshev|direct|bgs", + }, + ) + amg_coarsening_type: str = field( + default="HMIS", + metadata={ + "name": "amgCoarsening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|CLJP|RugeStueben|Falgout|PMIS|HMIS", + }, + ) + amg_interpolation_max_non_zeros: str = field( + default="4", + metadata={ + "name": "amgInterpolationMaxNonZeros", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_interpolation_type: str = field( + default="extendedI", + metadata={ + "name": "amgInterpolation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|modifiedClassical|direct|multipass|extendedI|standard|extended|directBAMG|modifiedExtended|modifiedExtendedI|modifiedExtendedE", + }, + ) + amg_null_space_type: str = field( + default="constantModes", + metadata={ + "name": "amgNullSpace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|constantModes|rigidBodyModes", + }, + ) + amg_num_functions: str = field( + default="1", + metadata={ + "name": "amgNumFunctions", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_num_sweeps: str = field( + default="1", + metadata={ + "name": "amgNumSweeps", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_relax_weight: str = field( + default="1", + metadata={ + "name": "amgRelaxWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + amg_separate_components: str = field( + default="0", + metadata={ + "name": "amgSeparateComponents", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_smoother_type: str = field( + default="l1sgs", + metadata={ + "name": "amgSmoother", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|jacobi|l1jacobi|fgs|bgs|sgs|l1sgs|chebyshev|ilu0|ilut|ic0|ict", + }, + ) + amg_threshold: str = field( + default="0", + metadata={ + "name": "amgThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direct_check_residual: str = field( + default="0", + metadata={ + "name": "directCheckResidual", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_col_perm: str = field( + default="metis", + metadata={ + "name": "directColPerm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|MMD_AtplusA|MMD_AtA|colAMD|metis|parmetis", + }, + ) + direct_equil: str = field( + default="1", + metadata={ + "name": "directEquil", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_iter_ref: str = field( + default="1", + metadata={ + "name": "directIterRef", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_parallel: str = field( + default="1", + metadata={ + "name": "directParallel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_repl_tiny_pivot: str = field( + default="1", + metadata={ + "name": "directReplTinyPivot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_row_perm: str = field( + default="mc64", + metadata={ + "name": "directRowPerm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|mc64", + }, + ) + ilu_fill: str = field( + default="0", + metadata={ + "name": "iluFill", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + ilu_threshold: str = field( + default="0", + metadata={ + "name": "iluThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + krylov_adaptive_tol: str = field( + default="0", + metadata={ + "name": "krylovAdaptiveTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_max_iter: str = field( + default="200", + metadata={ + "name": "krylovMaxIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_max_restart: str = field( + default="200", + metadata={ + "name": "krylovMaxRestart", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_tol: str = field( + default="1e-06", + metadata={ + "name": "krylovTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + krylov_weakest_tol: str = field( + default="0.001", + metadata={ + "name": "krylovWeakestTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + preconditioner_type: str = field( + default="iluk", + metadata={ + "name": "preconditioner", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|jacobi|l1jacobi|fgs|sgs|l1sgs|chebyshev|iluk|ilut|icc|ict|amg|mgr|block|direct|bgs", + }, + ) + solver_type: str = field( + default="direct", + metadata={ + "name": "solver", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|direct|cg|gmres|fgmres|bicgstab|preconditioner", + }, + ) + stop_if_error: str = field( + default="1", + metadata={ + "name": "stopIfError", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + + +class ModifiedCamClay(BaseModel): + class Meta: + name = "ModifiedCamClay" + + model_config = ConfigDict(defer_build=True) + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class MultiPhaseConstantThermalConductivity(BaseModel): + class Meta: + name = "MultiPhaseConstantThermalConductivity" + + model_config = ConfigDict(defer_build=True) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + thermal_conductivity_components: str = field( + metadata={ + "name": "thermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class MultiPhaseVolumeWeightedThermalConductivity(BaseModel): + class Meta: + name = "MultiPhaseVolumeWeightedThermalConductivity" + + model_config = ConfigDict(defer_build=True) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + phase_thermal_conductivity: str = field( + metadata={ + "name": "phaseThermalConductivity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + rock_thermal_conductivity_components: str = field( + metadata={ + "name": "rockThermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class MultiphasePoromechanicsInitialization(BaseModel): + class Meta: + name = "MultiphasePoromechanicsInitialization" + + model_config = ConfigDict(defer_build=True) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class MultivariableTableFunction(BaseModel): + class Meta: + name = "MultivariableTableFunction" + + model_config = ConfigDict(defer_build=True) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class NonlinearSolverParameters(BaseModel): + class Meta: + name = "NonlinearSolverParameters" + + model_config = ConfigDict(defer_build=True) + allow_non_converged: str = field( + default="0", + metadata={ + "name": "allowNonConverged", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + coupling_type: str = field( + default="FullyImplicit", + metadata={ + "name": "coupling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|FullyImplicit|Sequential", + }, + ) + line_search_action: str = field( + default="Attempt", + metadata={ + "name": "lineSearchAction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Attempt|Require", + }, + ) + line_search_cut_factor: str = field( + default="0.5", + metadata={ + "name": "lineSearchCutFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + line_search_interpolation_type: str = field( + default="Linear", + metadata={ + "name": "lineSearchInterpolation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Linear|Parabolic", + }, + ) + line_search_max_cuts: str = field( + default="4", + metadata={ + "name": "lineSearchMaxCuts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + line_search_starting_iteration: str = field( + default="0", + metadata={ + "name": "lineSearchStartingIteration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_allowed_residual_norm: str = field( + default="1e+09", + metadata={ + "name": "maxAllowedResidualNorm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_configuration_attempts: str = field( + default="10", + metadata={ + "name": "maxNumConfigurationAttempts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_sub_steps: str = field( + default="10", + metadata={ + "name": "maxSubSteps", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_time_step_cuts: str = field( + default="2", + metadata={ + "name": "maxTimeStepCuts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + min_normalizer: str = field( + default="1e-12", + metadata={ + "name": "minNormalizer", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newton_max_iter: str = field( + default="5", + metadata={ + "name": "newtonMaxIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newton_min_iter: str = field( + default="1", + metadata={ + "name": "newtonMinIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newton_tol: str = field( + default="1e-06", + metadata={ + "name": "newtonTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + nonlinear_acceleration_type: str = field( + default="None", + metadata={ + "name": "nonlinearAcceleration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Aitken", + }, + ) + sequential_convergence_criterion: str = field( + default="ResidualNorm", + metadata={ + "name": "sequentialConvergenceCriterion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|ResidualNorm|NumberOfNonlinearIterations|SolutionIncrements", + }, + ) + subcycling: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + time_step_cut_factor: str = field( + default="0.5", + metadata={ + "name": "timeStepCutFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_decrease_factor: str = field( + default="0.5", + metadata={ + "name": "timeStepDecreaseFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_decrease_iter_limit: str = field( + default="0.7", + metadata={ + "name": "timeStepDecreaseIterLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_increase_factor: str = field( + default="2", + metadata={ + "name": "timeStepIncreaseFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_increase_iter_limit: str = field( + default="0.4", + metadata={ + "name": "timeStepIncreaseIterLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + norm_type: str = field( + default="Linfinity", + metadata={ + "name": "norm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Linfinity|L2", + }, + ) + + +class NullModel(BaseModel): + class Meta: + name = "NullModel" + + model_config = ConfigDict(defer_build=True) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Pml(BaseModel): + class Meta: + name = "PML" + + model_config = ConfigDict(defer_build=True) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + reflectivity: str = field( + default="0.001", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + thickness_max_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "thicknessMaxXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + thickness_min_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "thicknessMinXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + wave_speed_max_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "waveSpeedMaxXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + wave_speed_min_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "waveSpeedMinXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_max: str = field( + default="{3.40282e+38,3.40282e+38,3.40282e+38}", + metadata={ + "name": "xMax", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_min: str = field( + default="{-3.40282e+38,-3.40282e+38,-3.40282e+38}", + metadata={ + "name": "xMin", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Pvtdriver(BaseModel): + class Meta: + name = "PVTDriver" + + model_config = ConfigDict(defer_build=True) + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + feed_composition: str = field( + metadata={ + "name": "feedComposition", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + fluid: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_compressibility: str = field( + default="0", + metadata={ + "name": "outputCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_phase_composition: str = field( + default="0", + metadata={ + "name": "outputPhaseComposition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + pressure_control: str = field( + metadata={ + "name": "pressureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + temperature_control: str = field( + metadata={ + "name": "temperatureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PackCollection(BaseModel): + class Meta: + name = "PackCollection" + + model_config = ConfigDict(defer_build=True) + disable_coord_collection: str = field( + default="0", + metadata={ + "name": "disableCoordCollection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + field_name: str = field( + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + object_path: str = field( + metadata={ + "name": "objectPath", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + only_on_set_change: str = field( + default="0", + metadata={ + "name": "onlyOnSetChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + set_names: str = field( + default="{}", + metadata={ + "name": "setNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ParallelPlatesPermeability(BaseModel): + class Meta: + name = "ParallelPlatesPermeability" + + model_config = ConfigDict(defer_build=True) + transversal_permeability: str = field( + default="-1", + metadata={ + "name": "transversalPermeability", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Parameter(BaseModel): + class Meta: + name = "Parameter" + + model_config = ConfigDict(defer_build=True) + value: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ParticleFluid(BaseModel): + class Meta: + name = "ParticleFluid" + + model_config = ConfigDict(defer_build=True) + collision_alpha: str = field( + default="1.27", + metadata={ + "name": "collisionAlpha", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + collision_beta: str = field( + default="1.5", + metadata={ + "name": "collisionBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + fluid_viscosity: str = field( + default="0.001", + metadata={ + "name": "fluidViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + hindered_settling_coefficient: str = field( + default="5.9", + metadata={ + "name": "hinderedSettlingCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_collisional_slip: str = field( + default="0", + metadata={ + "name": "isCollisionalSlip", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + particle_settling_model: str = field( + metadata={ + "name": "particleSettlingModel", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|Stokes|Intermediate|Turbulence", + } + ) + proppant_density: str = field( + default="1400", + metadata={ + "name": "proppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: str = field( + default="0.0002", + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + slip_concentration: str = field( + default="0.1", + metadata={ + "name": "slipConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + sphericity: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ParticleMesh(BaseModel): + class Meta: + name = "ParticleMesh" + + model_config = ConfigDict(defer_build=True) + header_file: str = field( + metadata={ + "name": "headerFile", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + } + ) + particle_block_names: str = field( + metadata={ + "name": "particleBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + particle_file: str = field( + metadata={ + "name": "particleFile", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + } + ) + particle_types: str = field( + metadata={ + "name": "particleTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ParticleRegion(BaseModel): + class Meta: + name = "ParticleRegion" + + model_config = ConfigDict(defer_build=True) + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + particle_blocks: str = field( + default="{}", + metadata={ + "name": "particleBlocks", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PerfectlyPlastic(BaseModel): + class Meta: + name = "PerfectlyPlastic" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_yield_stress: str = field( + default="1.79769e+308", + metadata={ + "name": "defaultYieldStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Perforation(BaseModel): + class Meta: + name = "Perforation" + + model_config = ConfigDict(defer_build=True) + distance_from_head: str = field( + metadata={ + "name": "distanceFromHead", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + skin_factor: str = field( + default="0", + metadata={ + "name": "skinFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + transmissibility: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PermeabilityBase(BaseModel): + class Meta: + name = "PermeabilityBase" + + model_config = ConfigDict(defer_build=True) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousDamageElasticIsotropic(BaseModel): + class Meta: + name = "PorousDamageElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousDamageSpectralElasticIsotropic(BaseModel): + class Meta: + name = "PorousDamageSpectralElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousDamageVolDevElasticIsotropic(BaseModel): + class Meta: + name = "PorousDamageVolDevElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousDelftEgg(BaseModel): + class Meta: + name = "PorousDelftEgg" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousDruckerPrager(BaseModel): + class Meta: + name = "PorousDruckerPrager" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousElasticIsotropic(BaseModel): + class Meta: + name = "PorousElasticIsotropic" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousElasticOrthotropic(BaseModel): + class Meta: + name = "PorousElasticOrthotropic" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousElasticTransverseIsotropic(BaseModel): + class Meta: + name = "PorousElasticTransverseIsotropic" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousExtendedDruckerPrager(BaseModel): + class Meta: + name = "PorousExtendedDruckerPrager" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousModifiedCamClay(BaseModel): + class Meta: + name = "PorousModifiedCamClay" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousViscoDruckerPrager(BaseModel): + class Meta: + name = "PorousViscoDruckerPrager" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousViscoExtendedDruckerPrager(BaseModel): + class Meta: + name = "PorousViscoExtendedDruckerPrager" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PorousViscoModifiedCamClay(BaseModel): + class Meta: + name = "PorousViscoModifiedCamClay" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PressurePorosity(BaseModel): + class Meta: + name = "PressurePorosity" + + model_config = ConfigDict(defer_build=True) + compressibility: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_reference_porosity: str = field( + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + reference_pressure: str = field( + metadata={ + "name": "referencePressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ProppantPermeability(BaseModel): + class Meta: + name = "ProppantPermeability" + + model_config = ConfigDict(defer_build=True) + max_proppant_concentration: str = field( + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + proppant_diameter: str = field( + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ProppantPorosity(BaseModel): + class Meta: + name = "ProppantPorosity" + + model_config = ConfigDict(defer_build=True) + default_reference_porosity: str = field( + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + max_proppant_concentration: str = field( + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ProppantSlurryFluid(BaseModel): + class Meta: + name = "ProppantSlurryFluid" + + model_config = ConfigDict(defer_build=True) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_component_density: str = field( + default="{0}", + metadata={ + "name": "defaultComponentDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + default_component_viscosity: str = field( + default="{0}", + metadata={ + "name": "defaultComponentViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + default_compressibility: str = field( + default="{0}", + metadata={ + "name": "defaultCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + flow_behavior_index: str = field( + default="{0}", + metadata={ + "name": "flowBehaviorIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + flow_consistency_index: str = field( + default="{0}", + metadata={ + "name": "flowConsistencyIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="100000", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_proppant_density: str = field( + default="1400", + metadata={ + "name": "referenceProppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ProppantSolidProppantPermeability(BaseModel): + class Meta: + name = "ProppantSolidProppantPermeability" + + model_config = ConfigDict(defer_build=True) + permeability_model_name: str = field( + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + porosity_model_name: str = field( + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: str = field( + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Python(BaseModel): + class Meta: + name = "Python" + + model_config = ConfigDict(defer_build=True) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ReactiveBrineThermal(BaseModel): + class Meta: + name = "ReactiveBrineThermal" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ReactiveBrine(BaseModel): + class Meta: + name = "ReactiveBrine" + + model_config = ConfigDict(defer_build=True) + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: str = field( + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ReactiveFluidDriver(BaseModel): + class Meta: + name = "ReactiveFluidDriver" + + model_config = ConfigDict(defer_build=True) + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + feed_composition: str = field( + metadata={ + "name": "feedComposition", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + fluid: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + pressure_control: str = field( + metadata={ + "name": "pressureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + temperature_control: str = field( + metadata={ + "name": "temperatureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Rectangle(BaseModel): + class Meta: + name = "Rectangle" + + model_config = ConfigDict(defer_build=True) + dimensions: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + length_vector: str = field( + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + origin: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: str = field( + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class RelpermDriver(BaseModel): + class Meta: + name = "RelpermDriver" + + model_config = ConfigDict(defer_build=True) + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + relperm: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Restart(BaseModel): + class Meta: + name = "Restart" + + model_config = ConfigDict(defer_build=True) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Run(BaseModel): + class Meta: + name = "Run" + + model_config = ConfigDict(defer_build=True) + args: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + auto_partition: Optional[str] = field( + default=None, + metadata={ + "name": "autoPartition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + mesh_sizes: str = field( + default="{0}", + metadata={ + "name": "meshSizes", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + nodes: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + scale_list: str = field( + default="{0}", + metadata={ + "name": "scaleList", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + scaling: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + tasks_per_node: str = field( + metadata={ + "name": "tasksPerNode", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + threads_per_task: str = field( + default="0", + metadata={ + "name": "threadsPerTask", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + time_limit: str = field( + default="0", + metadata={ + "name": "timeLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + + +class Silo(BaseModel): + class Meta: + name = "Silo" + + model_config = ConfigDict(defer_build=True) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + field_names: str = field( + default="{}", + metadata={ + "name": "fieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + only_plot_specified_field_names: str = field( + default="0", + metadata={ + "name": "onlyPlotSpecifiedFieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_file_root: str = field( + default="plot", + metadata={ + "name": "plotFileRoot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_cell_element_mesh: str = field( + default="1", + metadata={ + "name": "writeCellElementMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_edge_mesh: str = field( + default="0", + metadata={ + "name": "writeEdgeMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_femfaces: str = field( + default="0", + metadata={ + "name": "writeFEMFaces", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_face_element_mesh: str = field( + default="1", + metadata={ + "name": "writeFaceElementMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseConstantThermalConductivity(BaseModel): + class Meta: + name = "SinglePhaseConstantThermalConductivity" + + model_config = ConfigDict(defer_build=True) + thermal_conductivity_components: str = field( + metadata={ + "name": "thermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhasePoromechanicsInitialization(BaseModel): + class Meta: + name = "SinglePhasePoromechanicsInitialization" + + model_config = ConfigDict(defer_build=True) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseReservoirPoromechanicsInitialization(BaseModel): + class Meta: + name = "SinglePhaseReservoirPoromechanicsInitialization" + + model_config = ConfigDict(defer_build=True) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: str = field( + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseStatistics(BaseModel): + class Meta: + name = "SinglePhaseStatistics" + + model_config = ConfigDict(defer_build=True) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SlipDependentPermeability(BaseModel): + class Meta: + name = "SlipDependentPermeability" + + model_config = ConfigDict(defer_build=True) + initial_permeability: str = field( + metadata={ + "name": "initialPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + max_perm_multiplier: str = field( + metadata={ + "name": "maxPermMultiplier", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + shear_disp_threshold: str = field( + metadata={ + "name": "shearDispThreshold", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidInternalEnergy(BaseModel): + class Meta: + name = "SolidInternalEnergy" + + model_config = ConfigDict(defer_build=True) + reference_internal_energy: str = field( + metadata={ + "name": "referenceInternalEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + reference_temperature: str = field( + metadata={ + "name": "referenceTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + volumetric_heat_capacity: str = field( + metadata={ + "name": "volumetricHeatCapacity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsStateReset(BaseModel): + class Meta: + name = "SolidMechanicsStateReset" + + model_config = ConfigDict(defer_build=True) + disable_inelasticity: str = field( + default="0", + metadata={ + "name": "disableInelasticity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reset_displacements: str = field( + default="1", + metadata={ + "name": "resetDisplacements", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsStatistics(BaseModel): + class Meta: + name = "SolidMechanicsStatistics" + + model_config = ConfigDict(defer_build=True) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SourceFlux(BaseModel): + class Meta: + name = "SourceFlux" + + model_config = ConfigDict(defer_build=True) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SurfaceElementRegion(BaseModel): + class Meta: + name = "SurfaceElementRegion" + + model_config = ConfigDict(defer_build=True) + default_aperture: str = field( + metadata={ + "name": "defaultAperture", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + face_block: str = field( + default="FractureSubRegion", + metadata={ + "name": "faceBlock", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + sub_region_type: str = field( + default="faceElement", + metadata={ + "name": "subRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|faceElement|embeddedElement", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SymbolicFunction(BaseModel): + class Meta: + name = "SymbolicFunction" + + model_config = ConfigDict(defer_build=True) + expression: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + variable_names: str = field( + metadata={ + "name": "variableNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TableCapillaryPressure(BaseModel): + class Meta: + name = "TableCapillaryPressure" + + model_config = ConfigDict(defer_build=True) + non_wetting_intermediate_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "nonWettingIntermediateCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + wetting_intermediate_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingIntermediateCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_non_wetting_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingNonWettingCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TableFunction(BaseModel): + class Meta: + name = "TableFunction" + + model_config = ConfigDict(defer_build=True) + coordinate_files: str = field( + default="{}", + metadata={ + "name": "coordinateFiles", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|\s*\{\s*(([^*?<>\|:";,\s]+\s*,\s*)*[^*?<>\|:";,\s]+\s*)?\}\s*', + }, + ) + coordinates: str = field( + default="{0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + interpolation: str = field( + default="linear", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|linear|nearest|upper|lower", + }, + ) + values: str = field( + default="{0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + voxel_file: Optional[str] = field( + default=None, + metadata={ + "name": "voxelFile", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TableRelativePermeabilityHysteresis(BaseModel): + class Meta: + name = "TableRelativePermeabilityHysteresis" + + model_config = ConfigDict(defer_build=True) + drainage_non_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageNonWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + drainage_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + drainage_wetting_non_wetting_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageWettingNonWettingRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + imbibition_non_wetting_rel_perm_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "imbibitionNonWettingRelPermTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + imbibition_wetting_rel_perm_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "imbibitionWettingRelPermTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + jerauld_parameter_a: str = field( + default="0.1", + metadata={ + "name": "jerauldParameterA", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + jerauld_parameter_b: str = field( + default="0", + metadata={ + "name": "jerauldParameterB", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + killough_curvature_parameter: str = field( + default="1", + metadata={ + "name": "killoughCurvatureParameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + three_phase_interpolator: str = field( + default="BAKER", + metadata={ + "name": "threePhaseInterpolator", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|BAKER|STONEII", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TableRelativePermeability(BaseModel): + class Meta: + name = "TableRelativePermeability" + + model_config = ConfigDict(defer_build=True) + non_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "nonWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + three_phase_interpolator: str = field( + default="BAKER", + metadata={ + "name": "threePhaseInterpolator", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|BAKER|STONEII", + }, + ) + wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "wettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + wetting_non_wetting_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "wettingNonWettingRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ThermalCompressibleSinglePhaseFluid(BaseModel): + class Meta: + name = "ThermalCompressibleSinglePhaseFluid" + + model_config = ConfigDict(defer_build=True) + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_viscosity: str = field( + metadata={ + "name": "defaultViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + density_model_type: str = field( + default="linear", + metadata={ + "name": "densityModel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + internal_energy_model_type: str = field( + default="linear", + metadata={ + "name": "internalEnergyModel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_internal_energy: str = field( + default="0.001", + metadata={ + "name": "referenceInternalEnergy", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="0", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_temperature: str = field( + default="0", + metadata={ + "name": "referenceTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + specific_heat_capacity: str = field( + default="0", + metadata={ + "name": "specificHeatCapacity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + thermal_expansion_coeff: str = field( + default="0", + metadata={ + "name": "thermalExpansionCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosity_model_type: str = field( + default="linear", + metadata={ + "name": "viscosityModel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ThickPlane(BaseModel): + class Meta: + name = "ThickPlane" + + model_config = ConfigDict(defer_build=True) + normal: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + origin: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + } + ) + thickness: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TimeHistory(BaseModel): + class Meta: + name = "TimeHistory" + + model_config = ConfigDict(defer_build=True) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + filename: str = field( + default="TimeHistory", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + format: str = field( + default="hdf", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + sources: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Traction(BaseModel): + class Meta: + name = "Traction" + + model_config = ConfigDict(defer_build=True) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + input_stress: str = field( + default="{0,0,0,0,0,0}", + metadata={ + "name": "inputStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){5}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: str = field( + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + traction_type: str = field( + default="vector", + metadata={ + "name": "traction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|vector|normal|stress", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TriaxialDriver(BaseModel): + class Meta: + name = "TriaxialDriver" + + model_config = ConfigDict(defer_build=True) + axial_control: str = field( + metadata={ + "name": "axialControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + initial_stress: str = field( + metadata={ + "name": "initialStress", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + material: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + mode: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|mixedControl|strainControl|stressControl", + } + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + radial_control: str = field( + metadata={ + "name": "radialControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + steps: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class TwoPointFluxApproximation(BaseModel): + class Meta: + name = "TwoPointFluxApproximation" + + model_config = ConfigDict(defer_build=True) + area_rel_tol: str = field( + default="1e-08", + metadata={ + "name": "areaRelTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + mean_perm_coefficient: str = field( + default="1", + metadata={ + "name": "meanPermCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + upwinding_scheme: str = field( + default="PPU", + metadata={ + "name": "upwindingScheme", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|PPU|C1PPU|IHU", + }, + ) + use_pedfm: str = field( + default="0", + metadata={ + "name": "usePEDFM", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Vtk(BaseModel): + class Meta: + name = "VTK" + + model_config = ConfigDict(defer_build=True) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + field_names: str = field( + default="{}", + metadata={ + "name": "fieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + format: str = field( + default="binary", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|binary|ascii", + }, + ) + level_names: str = field( + default="{}", + metadata={ + "name": "levelNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + only_plot_specified_field_names: str = field( + default="0", + metadata={ + "name": "onlyPlotSpecifiedFieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_region_type: str = field( + default="all", + metadata={ + "name": "outputRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|cell|well|surface|particle|all", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_file_root: str = field( + default="VTK", + metadata={ + "name": "plotFileRoot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_femfaces: str = field( + default="0", + metadata={ + "name": "writeFEMFaces", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_ghost_cells: str = field( + default="0", + metadata={ + "name": "writeGhostCells", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class VanGenuchtenBakerRelativePermeability(BaseModel): + class Meta: + name = "VanGenuchtenBakerRelativePermeability" + + model_config = ConfigDict(defer_build=True) + gas_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "gasOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "waterOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class VanGenuchtenCapillaryPressure(BaseModel): + class Meta: + name = "VanGenuchtenCapillaryPressure" + + model_config = ConfigDict(defer_build=True) + cap_pressure_epsilon: str = field( + default="1e-06", + metadata={ + "name": "capPressureEpsilon", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_cap_pressure_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "phaseCapPressureExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_cap_pressure_multiplier: str = field( + default="{1}", + metadata={ + "name": "phaseCapPressureMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class VanGenuchtenStone2RelativePermeability(BaseModel): + class Meta: + name = "VanGenuchtenStone2RelativePermeability" + + model_config = ConfigDict(defer_build=True) + gas_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "gasOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: str = field( + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + water_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "waterOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ViscoDruckerPrager(BaseModel): + class Meta: + name = "ViscoDruckerPrager" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_angle: str = field( + default="30", + metadata={ + "name": "defaultDilationAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening_rate: str = field( + default="0", + metadata={ + "name": "defaultHardeningRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: str = field( + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ViscoExtendedDruckerPrager(BaseModel): + class Meta: + name = "ViscoExtendedDruckerPrager" + + model_config = ConfigDict(defer_build=True) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_dilation_ratio: str = field( + default="1", + metadata={ + "name": "defaultDilationRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening: str = field( + default="0", + metadata={ + "name": "defaultHardening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_initial_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultInitialFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_residual_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultResidualFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: str = field( + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ViscoModifiedCamClay(BaseModel): + class Meta: + name = "ViscoModifiedCamClay" + + model_config = ConfigDict(defer_build=True) + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: str = field( + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: str = field( + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class WellControls(BaseModel): + class Meta: + name = "WellControls" + + model_config = ConfigDict(defer_build=True) + control: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|BHP|phaseVolRate|totalVolRate|uninitialized", + } + ) + enable_crossflow: str = field( + default="1", + metadata={ + "name": "enableCrossflow", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_pressure_coefficient: str = field( + default="0.1", + metadata={ + "name": "initialPressureCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + injection_stream: str = field( + default="{-1}", + metadata={ + "name": "injectionStream", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + injection_temperature: str = field( + default="-1", + metadata={ + "name": "injectionTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reference_elevation: str = field( + metadata={ + "name": "referenceElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + status_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "statusTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + surface_pressure: str = field( + default="0", + metadata={ + "name": "surfacePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + surface_temperature: str = field( + default="0", + metadata={ + "name": "surfaceTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_bhp: str = field( + default="0", + metadata={ + "name": "targetBHP", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_bhptable_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetBHPTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_phase_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetPhaseName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_phase_rate: str = field( + default="0", + metadata={ + "name": "targetPhaseRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_rate_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetPhaseRateTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_total_rate: str = field( + default="0", + metadata={ + "name": "targetTotalRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_total_rate_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetTotalRateTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + type_value: str = field( + metadata={ + "name": "type", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|producer|injector", + } + ) + use_surface_conditions: str = field( + default="0", + metadata={ + "name": "useSurfaceConditions", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class WellElementRegion(BaseModel): + class Meta: + name = "WellElementRegion" + + model_config = ConfigDict(defer_build=True) + material_list: str = field( + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class WillisRichardsPermeability(BaseModel): + class Meta: + name = "WillisRichardsPermeability" + + model_config = ConfigDict(defer_build=True) + dilation_coefficient: str = field( + metadata={ + "name": "dilationCoefficient", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + max_frac_aperture: str = field( + metadata={ + "name": "maxFracAperture", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + ref_closure_stress: str = field( + metadata={ + "name": "refClosureStress", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class AcousticElasticSem(BaseModel): + class Meta: + name = "AcousticElasticSEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + acoustic_solver_name: str = field( + metadata={ + "name": "acousticSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + elastic_solver_name: str = field( + metadata={ + "name": "elasticSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class AcousticFirstOrderSem(BaseModel): + class Meta: + name = "AcousticFirstOrderSEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class AcousticSem(BaseModel): + class Meta: + name = "AcousticSEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class AcousticVtisem(BaseModel): + class Meta: + name = "AcousticVTISEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseFvm(BaseModel): + class Meta: + name = "CompositionalMultiphaseFVM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cont_multiplier_dbc: str = field( + default="0.5", + metadata={ + "name": "contMultiplierDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + continuation_dbc: str = field( + default="1", + metadata={ + "name": "continuationDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + kappamin_dbc: str = field( + default="1e-20", + metadata={ + "name": "kappaminDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="0.5", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_temperature_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativeTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_comp_dens_change: str = field( + default="1", + metadata={ + "name": "maxSequentialCompDensChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_comp_dens: str = field( + default="1e-10", + metadata={ + "name": "minCompDens", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + miscible_dbc: str = field( + default="0", + metadata={ + "name": "miscibleDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + omega_dbc: str = field( + default="1", + metadata={ + "name": "omegaDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + scaling_type: str = field( + default="Global", + metadata={ + "name": "scaling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Global|Local", + }, + ) + solution_change_scaling_factor: str = field( + default="0.5", + metadata={ + "name": "solutionChangeScalingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_flow_cfl: str = field( + default="-1", + metadata={ + "name": "targetFlowCFL", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_vol_fraction_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetPhaseVolFractionChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + target_relative_pressure_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativePressureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_relative_temperature_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativeTemperatureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + use_dbc: str = field( + default="0", + metadata={ + "name": "useDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_simple_accumulation: str = field( + default="1", + metadata={ + "name": "useSimpleAccumulation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_total_mass_equation: str = field( + default="1", + metadata={ + "name": "useTotalMassEquation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseHybridFvm(BaseModel): + class Meta: + name = "CompositionalMultiphaseHybridFVM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="0.5", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_temperature_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativeTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_comp_dens_change: str = field( + default="1", + metadata={ + "name": "maxSequentialCompDensChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_comp_dens: str = field( + default="1e-10", + metadata={ + "name": "minCompDens", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + solution_change_scaling_factor: str = field( + default="0.5", + metadata={ + "name": "solutionChangeScalingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_flow_cfl: str = field( + default="-1", + metadata={ + "name": "targetFlowCFL", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_vol_fraction_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetPhaseVolFractionChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + target_relative_pressure_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativePressureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_relative_temperature_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativeTemperatureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_simple_accumulation: str = field( + default="1", + metadata={ + "name": "useSimpleAccumulation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_total_mass_equation: str = field( + default="1", + metadata={ + "name": "useTotalMassEquation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseReservoirPoromechanics(BaseModel): + class Meta: + name = "CompositionalMultiphaseReservoirPoromechanics" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reservoir_and_wells_solver_name: str = field( + metadata={ + "name": "reservoirAndWellsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + stabilization_multiplier: str = field( + default="1", + metadata={ + "name": "stabilizationMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_region_names: str = field( + default="{}", + metadata={ + "name": "stabilizationRegionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + stabilization_type: str = field( + default="None", + metadata={ + "name": "stabilization", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Global|Local", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseReservoir(BaseModel): + class Meta: + name = "CompositionalMultiphaseReservoir" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class CompositionalMultiphaseWell(BaseModel): + class Meta: + name = "CompositionalMultiphaseWell" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + well_controls: List[WellControls] = field( + default_factory=list, + metadata={ + "name": "WellControls", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="1", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="1", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Constitutive(BaseModel): + class Meta: + name = "Constitutive" + + model_config = ConfigDict(defer_build=True) + biot_porosity: List[BiotPorosity] = field( + default_factory=list, + metadata={ + "name": "BiotPorosity", + "type": "Element", + "namespace": "", + }, + ) + black_oil_fluid: List[BlackOilFluid] = field( + default_factory=list, + metadata={ + "name": "BlackOilFluid", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_baker_relative_permeability: List[ + BrooksCoreyBakerRelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyBakerRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_capillary_pressure: List[BrooksCoreyCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_relative_permeability: List[BrooksCoreyRelativePermeability] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_stone2_relative_permeability: List[ + BrooksCoreyStone2RelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyStone2RelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_ezrokhi_fluid: List[Co2BrineEzrokhiFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrineEzrokhiFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_ezrokhi_thermal_fluid: List[Co2BrineEzrokhiThermalFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrineEzrokhiThermalFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_phillips_fluid: List[Co2BrinePhillipsFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrinePhillipsFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_phillips_thermal_fluid: List[Co2BrinePhillipsThermalFluid] = field( + default_factory=list, + metadata={ + "name": "CO2BrinePhillipsThermalFluid", + "type": "Element", + "namespace": "", + }, + ) + carman_kozeny_permeability: List[CarmanKozenyPermeability] = field( + default_factory=list, + metadata={ + "name": "CarmanKozenyPermeability", + "type": "Element", + "namespace": "", + }, + ) + ceramic_damage: List[CeramicDamage] = field( + default_factory=list, + metadata={ + "name": "CeramicDamage", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_fluid: List[CompositionalMultiphaseFluid] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseFluid", + "type": "Element", + "namespace": "", + }, + ) + compositonal_two_phase_fluid_peng_robinson: List[ + CompositonalTwoPhaseFluidPengRobinson + ] = field( + default_factory=list, + metadata={ + "name": "CompositonalTwoPhaseFluidPengRobinson", + "type": "Element", + "namespace": "", + }, + ) + compositonal_two_phase_fluid_soave_redlich_kwong: List[ + CompositonalTwoPhaseFluidSoaveRedlichKwong + ] = field( + default_factory=list, + metadata={ + "name": "CompositonalTwoPhaseFluidSoaveRedlichKwong", + "type": "Element", + "namespace": "", + }, + ) + compressible_single_phase_fluid: List[CompressibleSinglePhaseFluid] = field( + default_factory=list, + metadata={ + "name": "CompressibleSinglePhaseFluid", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_carman_kozeny_permeability: List[ + CompressibleSolidCarmanKozenyPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidCarmanKozenyPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_constant_permeability: List[ + CompressibleSolidConstantPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidConstantPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_exponential_decay_permeability: List[ + CompressibleSolidExponentialDecayPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidExponentialDecayPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_parallel_plates_permeability: List[ + CompressibleSolidParallelPlatesPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidParallelPlatesPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_slip_dependent_permeability: List[ + CompressibleSolidSlipDependentPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidSlipDependentPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_willis_richards_permeability: List[ + CompressibleSolidWillisRichardsPermeability + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidWillisRichardsPermeability", + "type": "Element", + "namespace": "", + }, + ) + constant_diffusion: List[ConstantDiffusion] = field( + default_factory=list, + metadata={ + "name": "ConstantDiffusion", + "type": "Element", + "namespace": "", + }, + ) + constant_permeability: List[ConstantPermeability] = field( + default_factory=list, + metadata={ + "name": "ConstantPermeability", + "type": "Element", + "namespace": "", + }, + ) + coulomb: List[Coulomb] = field( + default_factory=list, + metadata={ + "name": "Coulomb", + "type": "Element", + "namespace": "", + }, + ) + damage_elastic_isotropic: List[DamageElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "DamageElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + damage_spectral_elastic_isotropic: List[DamageSpectralElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "DamageSpectralElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + damage_vol_dev_elastic_isotropic: List[DamageVolDevElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "DamageVolDevElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + dead_oil_fluid: List[DeadOilFluid] = field( + default_factory=list, + metadata={ + "name": "DeadOilFluid", + "type": "Element", + "namespace": "", + }, + ) + delft_egg: List[DelftEgg] = field( + default_factory=list, + metadata={ + "name": "DelftEgg", + "type": "Element", + "namespace": "", + }, + ) + drucker_prager: List[DruckerPrager] = field( + default_factory=list, + metadata={ + "name": "DruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + elastic_isotropic: List[ElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "ElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + elastic_isotropic_pressure_dependent: List[ElasticIsotropicPressureDependent] = ( + field( + default_factory=list, + metadata={ + "name": "ElasticIsotropicPressureDependent", + "type": "Element", + "namespace": "", + }, + ) + ) + elastic_orthotropic: List[ElasticOrthotropic] = field( + default_factory=list, + metadata={ + "name": "ElasticOrthotropic", + "type": "Element", + "namespace": "", + }, + ) + elastic_transverse_isotropic: List[ElasticTransverseIsotropic] = field( + default_factory=list, + metadata={ + "name": "ElasticTransverseIsotropic", + "type": "Element", + "namespace": "", + }, + ) + exponential_decay_permeability: List[ExponentialDecayPermeability] = field( + default_factory=list, + metadata={ + "name": "ExponentialDecayPermeability", + "type": "Element", + "namespace": "", + }, + ) + extended_drucker_prager: List[ExtendedDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "ExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + frictionless_contact: List[FrictionlessContact] = field( + default_factory=list, + metadata={ + "name": "FrictionlessContact", + "type": "Element", + "namespace": "", + }, + ) + jfunction_capillary_pressure: List[JfunctionCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "JFunctionCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + linear_isotropic_dispersion: List[LinearIsotropicDispersion] = field( + default_factory=list, + metadata={ + "name": "LinearIsotropicDispersion", + "type": "Element", + "namespace": "", + }, + ) + modified_cam_clay: List[ModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "ModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + multi_phase_constant_thermal_conductivity: List[ + MultiPhaseConstantThermalConductivity + ] = field( + default_factory=list, + metadata={ + "name": "MultiPhaseConstantThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + multi_phase_volume_weighted_thermal_conductivity: List[ + MultiPhaseVolumeWeightedThermalConductivity + ] = field( + default_factory=list, + metadata={ + "name": "MultiPhaseVolumeWeightedThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + null_model: List[NullModel] = field( + default_factory=list, + metadata={ + "name": "NullModel", + "type": "Element", + "namespace": "", + }, + ) + parallel_plates_permeability: List[ParallelPlatesPermeability] = field( + default_factory=list, + metadata={ + "name": "ParallelPlatesPermeability", + "type": "Element", + "namespace": "", + }, + ) + particle_fluid: List[ParticleFluid] = field( + default_factory=list, + metadata={ + "name": "ParticleFluid", + "type": "Element", + "namespace": "", + }, + ) + perfectly_plastic: List[PerfectlyPlastic] = field( + default_factory=list, + metadata={ + "name": "PerfectlyPlastic", + "type": "Element", + "namespace": "", + }, + ) + permeability_base: List[PermeabilityBase] = field( + default_factory=list, + metadata={ + "name": "PermeabilityBase", + "type": "Element", + "namespace": "", + }, + ) + porous_damage_elastic_isotropic: List[PorousDamageElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "PorousDamageElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_damage_spectral_elastic_isotropic: List[ + PorousDamageSpectralElasticIsotropic + ] = field( + default_factory=list, + metadata={ + "name": "PorousDamageSpectralElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_damage_vol_dev_elastic_isotropic: List[ + PorousDamageVolDevElasticIsotropic + ] = field( + default_factory=list, + metadata={ + "name": "PorousDamageVolDevElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_delft_egg: List[PorousDelftEgg] = field( + default_factory=list, + metadata={ + "name": "PorousDelftEgg", + "type": "Element", + "namespace": "", + }, + ) + porous_drucker_prager: List[PorousDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "PorousDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_isotropic: List[PorousElasticIsotropic] = field( + default_factory=list, + metadata={ + "name": "PorousElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_orthotropic: List[PorousElasticOrthotropic] = field( + default_factory=list, + metadata={ + "name": "PorousElasticOrthotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_transverse_isotropic: List[PorousElasticTransverseIsotropic] = field( + default_factory=list, + metadata={ + "name": "PorousElasticTransverseIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_extended_drucker_prager: List[PorousExtendedDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "PorousExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_modified_cam_clay: List[PorousModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "PorousModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + porous_visco_drucker_prager: List[PorousViscoDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "PorousViscoDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_visco_extended_drucker_prager: List[PorousViscoExtendedDruckerPrager] = ( + field( + default_factory=list, + metadata={ + "name": "PorousViscoExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + ) + porous_visco_modified_cam_clay: List[PorousViscoModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "PorousViscoModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + pressure_porosity: List[PressurePorosity] = field( + default_factory=list, + metadata={ + "name": "PressurePorosity", + "type": "Element", + "namespace": "", + }, + ) + proppant_permeability: List[ProppantPermeability] = field( + default_factory=list, + metadata={ + "name": "ProppantPermeability", + "type": "Element", + "namespace": "", + }, + ) + proppant_porosity: List[ProppantPorosity] = field( + default_factory=list, + metadata={ + "name": "ProppantPorosity", + "type": "Element", + "namespace": "", + }, + ) + proppant_slurry_fluid: List[ProppantSlurryFluid] = field( + default_factory=list, + metadata={ + "name": "ProppantSlurryFluid", + "type": "Element", + "namespace": "", + }, + ) + proppant_solid_proppant_permeability: List[ProppantSolidProppantPermeability] = ( + field( + default_factory=list, + metadata={ + "name": "ProppantSolidProppantPermeability", + "type": "Element", + "namespace": "", + }, + ) + ) + reactive_brine: List[ReactiveBrine] = field( + default_factory=list, + metadata={ + "name": "ReactiveBrine", + "type": "Element", + "namespace": "", + }, + ) + reactive_brine_thermal: List[ReactiveBrineThermal] = field( + default_factory=list, + metadata={ + "name": "ReactiveBrineThermal", + "type": "Element", + "namespace": "", + }, + ) + single_phase_constant_thermal_conductivity: List[ + SinglePhaseConstantThermalConductivity + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseConstantThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + slip_dependent_permeability: List[SlipDependentPermeability] = field( + default_factory=list, + metadata={ + "name": "SlipDependentPermeability", + "type": "Element", + "namespace": "", + }, + ) + solid_internal_energy: List[SolidInternalEnergy] = field( + default_factory=list, + metadata={ + "name": "SolidInternalEnergy", + "type": "Element", + "namespace": "", + }, + ) + table_capillary_pressure: List[TableCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "TableCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + table_relative_permeability: List[TableRelativePermeability] = field( + default_factory=list, + metadata={ + "name": "TableRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + table_relative_permeability_hysteresis: List[ + TableRelativePermeabilityHysteresis + ] = field( + default_factory=list, + metadata={ + "name": "TableRelativePermeabilityHysteresis", + "type": "Element", + "namespace": "", + }, + ) + thermal_compressible_single_phase_fluid: List[ + ThermalCompressibleSinglePhaseFluid + ] = field( + default_factory=list, + metadata={ + "name": "ThermalCompressibleSinglePhaseFluid", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_baker_relative_permeability: List[ + VanGenuchtenBakerRelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenBakerRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_capillary_pressure: List[VanGenuchtenCapillaryPressure] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_stone2_relative_permeability: List[ + VanGenuchtenStone2RelativePermeability + ] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenStone2RelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + visco_drucker_prager: List[ViscoDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "ViscoDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + visco_extended_drucker_prager: List[ViscoExtendedDruckerPrager] = field( + default_factory=list, + metadata={ + "name": "ViscoExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + visco_modified_cam_clay: List[ViscoModifiedCamClay] = field( + default_factory=list, + metadata={ + "name": "ViscoModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + willis_richards_permeability: List[WillisRichardsPermeability] = field( + default_factory=list, + metadata={ + "name": "WillisRichardsPermeability", + "type": "Element", + "namespace": "", + }, + ) + + +class ElasticFirstOrderSem(BaseModel): + class Meta: + name = "ElasticFirstOrderSEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ElasticSem(BaseModel): + class Meta: + name = "ElasticSEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + linear_dassamples: str = field( + default="5", + metadata={ + "name": "linearDASSamples", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + source_force: str = field( + default="{0,0,0}", + metadata={ + "name": "sourceForce", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + source_moment: str = field( + default="{1,1,1,0,0,0}", + metadata={ + "name": "sourceMoment", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){5}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_das: str = field( + default="none", + metadata={ + "name": "useDAS", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|dipole|strainIntegration", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ElementRegions(BaseModel): + class Meta: + name = "ElementRegions" + + model_config = ConfigDict(defer_build=True) + cell_element_region: List[CellElementRegion] = field( + default_factory=list, + metadata={ + "name": "CellElementRegion", + "type": "Element", + "namespace": "", + }, + ) + surface_element_region: List[SurfaceElementRegion] = field( + default_factory=list, + metadata={ + "name": "SurfaceElementRegion", + "type": "Element", + "namespace": "", + }, + ) + well_element_region: List[WellElementRegion] = field( + default_factory=list, + metadata={ + "name": "WellElementRegion", + "type": "Element", + "namespace": "", + }, + ) + + +class EmbeddedSurfaceGenerator(BaseModel): + class Meta: + name = "EmbeddedSurfaceGenerator" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + fracture_region: str = field( + default="FractureRegion", + metadata={ + "name": "fractureRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mpi_comm_order: str = field( + default="0", + metadata={ + "name": "mpiCommOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_objects: str = field( + metadata={ + "name": "targetObjects", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class FieldSpecifications(BaseModel): + class Meta: + name = "FieldSpecifications" + + model_config = ConfigDict(defer_build=True) + aquifer: List[Aquifer] = field( + default_factory=list, + metadata={ + "name": "Aquifer", + "type": "Element", + "namespace": "", + }, + ) + dirichlet: List[Dirichlet] = field( + default_factory=list, + metadata={ + "name": "Dirichlet", + "type": "Element", + "namespace": "", + }, + ) + field_specification: List[FieldSpecification] = field( + default_factory=list, + metadata={ + "name": "FieldSpecification", + "type": "Element", + "namespace": "", + }, + ) + hydrostatic_equilibrium: List[HydrostaticEquilibrium] = field( + default_factory=list, + metadata={ + "name": "HydrostaticEquilibrium", + "type": "Element", + "namespace": "", + }, + ) + pml: List[Pml] = field( + default_factory=list, + metadata={ + "name": "PML", + "type": "Element", + "namespace": "", + }, + ) + source_flux: List[SourceFlux] = field( + default_factory=list, + metadata={ + "name": "SourceFlux", + "type": "Element", + "namespace": "", + }, + ) + traction: List[Traction] = field( + default_factory=list, + metadata={ + "name": "Traction", + "type": "Element", + "namespace": "", + }, + ) + + +class FiniteElements(BaseModel): + class Meta: + name = "FiniteElements" + + model_config = ConfigDict(defer_build=True) + finite_element_space: List[FiniteElementSpace] = field( + default_factory=list, + metadata={ + "name": "FiniteElementSpace", + "type": "Element", + "namespace": "", + }, + ) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + + +class FiniteVolume(BaseModel): + class Meta: + name = "FiniteVolume" + + model_config = ConfigDict(defer_build=True) + hybrid_mimetic_discretization: List[HybridMimeticDiscretization] = field( + default_factory=list, + metadata={ + "name": "HybridMimeticDiscretization", + "type": "Element", + "namespace": "", + }, + ) + two_point_flux_approximation: List[TwoPointFluxApproximation] = field( + default_factory=list, + metadata={ + "name": "TwoPointFluxApproximation", + "type": "Element", + "namespace": "", + }, + ) + + +class FlowProppantTransport(BaseModel): + class Meta: + name = "FlowProppantTransport" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + proppant_solver_name: str = field( + metadata={ + "name": "proppantSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Functions(BaseModel): + class Meta: + name = "Functions" + + model_config = ConfigDict(defer_build=True) + composite_function: List[CompositeFunction] = field( + default_factory=list, + metadata={ + "name": "CompositeFunction", + "type": "Element", + "namespace": "", + }, + ) + multivariable_table_function: List[MultivariableTableFunction] = field( + default_factory=list, + metadata={ + "name": "MultivariableTableFunction", + "type": "Element", + "namespace": "", + }, + ) + symbolic_function: List[SymbolicFunction] = field( + default_factory=list, + metadata={ + "name": "SymbolicFunction", + "type": "Element", + "namespace": "", + }, + ) + table_function: List[TableFunction] = field( + default_factory=list, + metadata={ + "name": "TableFunction", + "type": "Element", + "namespace": "", + }, + ) + + +class Geometry(BaseModel): + class Meta: + name = "Geometry" + + model_config = ConfigDict(defer_build=True) + box: List[Box] = field( + default_factory=list, + metadata={ + "name": "Box", + "type": "Element", + "namespace": "", + }, + ) + custom_polar_object: List[CustomPolarObject] = field( + default_factory=list, + metadata={ + "name": "CustomPolarObject", + "type": "Element", + "namespace": "", + }, + ) + cylinder: List[Cylinder] = field( + default_factory=list, + metadata={ + "name": "Cylinder", + "type": "Element", + "namespace": "", + }, + ) + disc: List[Disc] = field( + default_factory=list, + metadata={ + "name": "Disc", + "type": "Element", + "namespace": "", + }, + ) + rectangle: List[Rectangle] = field( + default_factory=list, + metadata={ + "name": "Rectangle", + "type": "Element", + "namespace": "", + }, + ) + thick_plane: List[ThickPlane] = field( + default_factory=list, + metadata={ + "name": "ThickPlane", + "type": "Element", + "namespace": "", + }, + ) + + +class Hydrofracture(BaseModel): + class Meta: + name = "Hydrofracture" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_matrix_poroelastic: str = field( + default="0", + metadata={ + "name": "isMatrixPoroelastic", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + surface_generator_name: str = field( + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + use_quasi_newton: str = field( + default="0", + metadata={ + "name": "useQuasiNewton", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Included(BaseModel): + class Meta: + name = "Included" + + model_config = ConfigDict(defer_build=True) + file: List[File] = field( + default_factory=list, + metadata={ + "name": "File", + "type": "Element", + "namespace": "", + }, + ) + + +class InternalWell(BaseModel): + class Meta: + name = "InternalWell" + + model_config = ConfigDict(defer_build=True) + perforation: List[Perforation] = field( + default_factory=list, + metadata={ + "name": "Perforation", + "type": "Element", + "namespace": "", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + min_element_length: str = field( + default="0.001", + metadata={ + "name": "minElementLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_segment_length: str = field( + default="0.01", + metadata={ + "name": "minSegmentLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_elements_per_segment: str = field( + metadata={ + "name": "numElementsPerSegment", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + polyline_node_coords: str = field( + metadata={ + "name": "polylineNodeCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + } + ) + polyline_segment_conn: str = field( + metadata={ + "name": "polylineSegmentConn", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*\}\s*", + } + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + well_controls_name: str = field( + metadata={ + "name": "wellControlsName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + well_region_name: str = field( + metadata={ + "name": "wellRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class LaplaceFem(BaseModel): + class Meta: + name = "LaplaceFEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + field_name: str = field( + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|SteadyState|ImplicitTransient", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class MultiphasePoromechanicsReservoir(BaseModel): + class Meta: + name = "MultiphasePoromechanicsReservoir" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class MultiphasePoromechanics(BaseModel): + class Meta: + name = "MultiphasePoromechanics" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + stabilization_multiplier: str = field( + default="1", + metadata={ + "name": "stabilizationMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_region_names: str = field( + default="{}", + metadata={ + "name": "stabilizationRegionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + stabilization_type: str = field( + default="None", + metadata={ + "name": "stabilization", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Global|Local", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Outputs(BaseModel): + class Meta: + name = "Outputs" + + model_config = ConfigDict(defer_build=True) + blueprint: List[Blueprint] = field( + default_factory=list, + metadata={ + "name": "Blueprint", + "type": "Element", + "namespace": "", + }, + ) + chombo_io: List[ChomboIo] = field( + default_factory=list, + metadata={ + "name": "ChomboIO", + "type": "Element", + "namespace": "", + }, + ) + python: List[Python] = field( + default_factory=list, + metadata={ + "name": "Python", + "type": "Element", + "namespace": "", + }, + ) + restart: List[Restart] = field( + default_factory=list, + metadata={ + "name": "Restart", + "type": "Element", + "namespace": "", + }, + ) + silo: List[Silo] = field( + default_factory=list, + metadata={ + "name": "Silo", + "type": "Element", + "namespace": "", + }, + ) + time_history: List[TimeHistory] = field( + default_factory=list, + metadata={ + "name": "TimeHistory", + "type": "Element", + "namespace": "", + }, + ) + vtk: List[Vtk] = field( + default_factory=list, + metadata={ + "name": "VTK", + "type": "Element", + "namespace": "", + }, + ) + + +class Parameters(BaseModel): + class Meta: + name = "Parameters" + + model_config = ConfigDict(defer_build=True) + parameter: List[Parameter] = field( + default_factory=list, + metadata={ + "name": "Parameter", + "type": "Element", + "namespace": "", + }, + ) + + +class ParticleRegions(BaseModel): + class Meta: + name = "ParticleRegions" + + model_config = ConfigDict(defer_build=True) + particle_region: List[ParticleRegion] = field( + default_factory=list, + metadata={ + "name": "ParticleRegion", + "type": "Element", + "namespace": "", + }, + ) + + +class PeriodicEvent(BaseModel): + class Meta: + name = "PeriodicEvent" + + model_config = ConfigDict(defer_build=True) + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List["PeriodicEvent"] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List["SoloEvent"] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cycle_frequency: str = field( + default="1", + metadata={ + "name": "cycleFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + object_value: Optional[str] = field( + default=None, + metadata={ + "name": "object", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + set: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + stat: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_timestep: str = field( + default="1", + metadata={ + "name": "targetExactTimestep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + threshold: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_frequency: str = field( + default="-1", + metadata={ + "name": "timeFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PhaseFieldDamageFem(BaseModel): + class Meta: + name = "PhaseFieldDamageFEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + damage_upper_bound: str = field( + default="1.5", + metadata={ + "name": "damageUpperBound", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + field_name: str = field( + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + irreversibility_flag: str = field( + default="0", + metadata={ + "name": "irreversibilityFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + local_dissipation: str = field( + metadata={ + "name": "localDissipation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|Linear|Quadratic", + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|SteadyState|ImplicitTransient|ExplicitTransient", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class PhaseFieldFracture(BaseModel): + class Meta: + name = "PhaseFieldFracture" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + damage_solver_name: str = field( + metadata={ + "name": "damageSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ProppantTransport(BaseModel): + class Meta: + name = "ProppantTransport" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + bridging_factor: str = field( + default="0", + metadata={ + "name": "bridgingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_shields_number: str = field( + default="0", + metadata={ + "name": "criticalShieldsNumber", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + friction_coefficient: str = field( + default="0.03", + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_density: str = field( + default="2500", + metadata={ + "name": "proppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: str = field( + default="0.0004", + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + update_proppant_packing: str = field( + default="0", + metadata={ + "name": "updateProppantPacking", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class ReactiveCompositionalMultiphaseObl(BaseModel): + class Meta: + name = "ReactiveCompositionalMultiphaseOBL" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + obloperators_table_file: str = field( + metadata={ + "name": "OBLOperatorsTableFile", + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + } + ) + allow_local_oblchopping: str = field( + default="1", + metadata={ + "name": "allowLocalOBLChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + enable_energy_balance: str = field( + metadata={ + "name": "enableEnergyBalance", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="1", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_components: str = field( + metadata={ + "name": "numComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + num_phases: str = field( + metadata={ + "name": "numPhases", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + trans_mult_exp: str = field( + default="1", + metadata={ + "name": "transMultExp", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_dartsl2_norm: str = field( + default="1", + metadata={ + "name": "useDARTSL2Norm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseFvm(BaseModel): + class Meta: + name = "SinglePhaseFVM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseHybridFvm(BaseModel): + class Meta: + name = "SinglePhaseHybridFVM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhasePoromechanicsConformingFractures(BaseModel): + class Meta: + name = "SinglePhasePoromechanicsConformingFractures" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhasePoromechanicsEmbeddedFractures(BaseModel): + class Meta: + name = "SinglePhasePoromechanicsEmbeddedFractures" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhasePoromechanicsReservoir(BaseModel): + class Meta: + name = "SinglePhasePoromechanicsReservoir" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: str = field( + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhasePoromechanics(BaseModel): + class Meta: + name = "SinglePhasePoromechanics" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseProppantFvm(BaseModel): + class Meta: + name = "SinglePhaseProppantFVM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_pressure_change: str = field( + default="100000", + metadata={ + "name": "maxSequentialPressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_sequential_temperature_change: str = field( + default="0.1", + metadata={ + "name": "maxSequentialTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseReservoirPoromechanics(BaseModel): + class Meta: + name = "SinglePhaseReservoirPoromechanics" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reservoir_and_wells_solver_name: str = field( + metadata={ + "name": "reservoirAndWellsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + solid_solver_name: str = field( + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseReservoir(BaseModel): + class Meta: + name = "SinglePhaseReservoir" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: str = field( + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + well_solver_name: str = field( + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SinglePhaseWell(BaseModel): + class Meta: + name = "SinglePhaseWell" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + well_controls: List[WellControls] = field( + default_factory=list, + metadata={ + "name": "WellControls", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + write_csv: str = field( + default="0", + metadata={ + "name": "writeCSV", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsEmbeddedFractures(BaseModel): + class Meta: + name = "SolidMechanicsEmbeddedFractures" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + use_static_condensation: str = field( + default="0", + metadata={ + "name": "useStaticCondensation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsLagrangeContact(BaseModel): + class Meta: + name = "SolidMechanicsLagrangeContact" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_name: str = field( + metadata={ + "name": "stabilizationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsLagrangianSsle(BaseModel): + class Meta: + name = "SolidMechanicsLagrangianSSLE" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + default="NOCONTACT", + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsLagrangianFem(BaseModel): + class Meta: + name = "SolidMechanics_LagrangianFEM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + default="NOCONTACT", + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SolidMechanicsMpm(BaseModel): + class Meta: + name = "SolidMechanics_MPM" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + boundary_condition_types: str = field( + default="{0}", + metadata={ + "name": "boundaryConditionTypes", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + box_average_history: str = field( + default="0", + metadata={ + "name": "boxAverageHistory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_gap_correction: str = field( + default="0", + metadata={ + "name": "contactGapCorrection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cpdi_domain_scaling: str = field( + default="0", + metadata={ + "name": "cpdiDomainScaling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + damage_field_partitioning: str = field( + default="0", + metadata={ + "name": "damageFieldPartitioning", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + discretization: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + } + ) + f_table_interp_type: str = field( + default="0", + metadata={ + "name": "fTableInterp", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + f_table_path: Optional[str] = field( + default=None, + metadata={ + "name": "fTablePath", + "type": "Attribute", + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + }, + ) + friction_coefficient: str = field( + default="0", + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + needs_neighbor_list: str = field( + default="0", + metadata={ + "name": "needsNeighborList", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + neighbor_radius: str = field( + default="-1", + metadata={ + "name": "neighborRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + plane_strain: str = field( + default="0", + metadata={ + "name": "planeStrain", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + prescribed_bc_table: str = field( + default="0", + metadata={ + "name": "prescribedBcTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + prescribed_boundary_ftable: str = field( + default="0", + metadata={ + "name": "prescribedBoundaryFTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reaction_history: str = field( + default="0", + metadata={ + "name": "reactionHistory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + separability_min_damage: str = field( + default="0.5", + metadata={ + "name": "separabilityMinDamage", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + solver_profiling: str = field( + default="0", + metadata={ + "name": "solverProfiling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_detection: str = field( + default="0", + metadata={ + "name": "surfaceDetection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + treat_fully_damaged_as_single_field: str = field( + default="1", + metadata={ + "name": "treatFullyDamagedAsSingleField", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_damage_as_surface_flag: str = field( + default="0", + metadata={ + "name": "useDamageAsSurfaceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class SurfaceGenerator(BaseModel): + class Meta: + name = "SurfaceGenerator" + + model_config = ConfigDict(defer_build=True) + linear_solver_parameters: List[LinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: List[NonlinearSolverParameters] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + fracture_region: str = field( + default="Fracture", + metadata={ + "name": "fractureRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_poroelastic: str = field( + default="0", + metadata={ + "name": "isPoroelastic", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mpi_comm_order: str = field( + default="0", + metadata={ + "name": "mpiCommOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + node_based_sif: str = field( + default="0", + metadata={ + "name": "nodeBasedSIF", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + rock_toughness: str = field( + metadata={ + "name": "rockToughness", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + target_regions: str = field( + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Tasks(BaseModel): + class Meta: + name = "Tasks" + + model_config = ConfigDict(defer_build=True) + compositional_multiphase_reservoir_poromechanics_initialization: List[ + CompositionalMultiphaseReservoirPoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoirPoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_statistics: List[CompositionalMultiphaseStatistics] = ( + field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseStatistics", + "type": "Element", + "namespace": "", + }, + ) + ) + multiphase_poromechanics_initialization: List[ + MultiphasePoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + pvtdriver: List[Pvtdriver] = field( + default_factory=list, + metadata={ + "name": "PVTDriver", + "type": "Element", + "namespace": "", + }, + ) + pack_collection: List[PackCollection] = field( + default_factory=list, + metadata={ + "name": "PackCollection", + "type": "Element", + "namespace": "", + }, + ) + reactive_fluid_driver: List[ReactiveFluidDriver] = field( + default_factory=list, + metadata={ + "name": "ReactiveFluidDriver", + "type": "Element", + "namespace": "", + }, + ) + relperm_driver: List[RelpermDriver] = field( + default_factory=list, + metadata={ + "name": "RelpermDriver", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_initialization: List[ + SinglePhasePoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir_poromechanics_initialization: List[ + SinglePhaseReservoirPoromechanicsInitialization + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoirPoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + single_phase_statistics: List[SinglePhaseStatistics] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseStatistics", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_state_reset: List[SolidMechanicsStateReset] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsStateReset", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_statistics: List[SolidMechanicsStatistics] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsStatistics", + "type": "Element", + "namespace": "", + }, + ) + triaxial_driver: List[TriaxialDriver] = field( + default_factory=list, + metadata={ + "name": "TriaxialDriver", + "type": "Element", + "namespace": "", + }, + ) + + +class Vtkwell(BaseModel): + class Meta: + name = "VTKWell" + + model_config = ConfigDict(defer_build=True) + perforation: List[Perforation] = field( + default_factory=list, + metadata={ + "name": "Perforation", + "type": "Element", + "namespace": "", + }, + ) + file: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + } + ) + min_element_length: str = field( + default="0.001", + metadata={ + "name": "minElementLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_segment_length: str = field( + default="0.01", + metadata={ + "name": "minSegmentLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_elements_per_segment: str = field( + metadata={ + "name": "numElementsPerSegment", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + } + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + } + ) + well_controls_name: str = field( + metadata={ + "name": "wellControlsName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + well_region_name: str = field( + metadata={ + "name": "wellRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Crusher(BaseModel): + class Meta: + name = "crusher" + + model_config = ConfigDict(defer_build=True) + run: List[Run] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +class Lassen(BaseModel): + class Meta: + name = "lassen" + + model_config = ConfigDict(defer_build=True) + run: List[Run] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +class Quartz(BaseModel): + class Meta: + name = "quartz" + + model_config = ConfigDict(defer_build=True) + run: List[Run] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +class Benchmarks(BaseModel): + class Meta: + name = "Benchmarks" + + model_config = ConfigDict(defer_build=True) + crusher: List[Crusher] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + lassen: List[Lassen] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + quartz: List[Quartz] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + + +class InternalMesh(BaseModel): + class Meta: + name = "InternalMesh" + + model_config = ConfigDict(defer_build=True) + internal_well: List[InternalWell] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + vtkwell: List[Vtkwell] = field( + default_factory=list, + metadata={ + "name": "VTKWell", + "type": "Element", + "namespace": "", + }, + ) + cell_block_names: str = field( + metadata={ + "name": "cellBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + element_types: str = field( + metadata={ + "name": "elementTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + nx: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + ny: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + nz: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + position_tolerance: str = field( + default="1e-10", + metadata={ + "name": "positionTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + triangle_pattern: str = field( + default="0", + metadata={ + "name": "trianglePattern", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + x_bias: str = field( + default="{1}", + metadata={ + "name": "xBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + x_coords: str = field( + metadata={ + "name": "xCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + y_bias: str = field( + default="{1}", + metadata={ + "name": "yBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_coords: str = field( + metadata={ + "name": "yCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + z_bias: str = field( + default="{1}", + metadata={ + "name": "zBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_coords: str = field( + metadata={ + "name": "zCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class InternalWellbore(BaseModel): + class Meta: + name = "InternalWellbore" + + model_config = ConfigDict(defer_build=True) + internal_well: List[InternalWell] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + vtkwell: List[Vtkwell] = field( + default_factory=list, + metadata={ + "name": "VTKWell", + "type": "Element", + "namespace": "", + }, + ) + auto_space_radial_elems: str = field( + default="{-1}", + metadata={ + "name": "autoSpaceRadialElems", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + cartesian_mapping_inner_radius: str = field( + default="1e+99", + metadata={ + "name": "cartesianMappingInnerRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cell_block_names: str = field( + metadata={ + "name": "cellBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + } + ) + element_types: str = field( + metadata={ + "name": "elementTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + } + ) + hard_radial_coords: str = field( + default="{0}", + metadata={ + "name": "hardRadialCoords", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + nr: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + nt: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + nz: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + } + ) + position_tolerance: str = field( + default="1e-10", + metadata={ + "name": "positionTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + r_bias: str = field( + default="{-0.8}", + metadata={ + "name": "rBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + radius: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + theta: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + trajectory: str = field( + default="{{0}}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + triangle_pattern: str = field( + default="0", + metadata={ + "name": "trianglePattern", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_cartesian_outer_boundary: str = field( + default="1000000", + metadata={ + "name": "useCartesianOuterBoundary", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + x_bias: str = field( + default="{1}", + metadata={ + "name": "xBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_bias: str = field( + default="{1}", + metadata={ + "name": "yBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_bias: str = field( + default="{1}", + metadata={ + "name": "zBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_coords: str = field( + metadata={ + "name": "zCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + } + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class NumericalMethods(BaseModel): + class Meta: + name = "NumericalMethods" + + model_config = ConfigDict(defer_build=True) + finite_elements: List[FiniteElements] = field( + default_factory=list, + metadata={ + "name": "FiniteElements", + "type": "Element", + "namespace": "", + }, + ) + finite_volume: List[FiniteVolume] = field( + default_factory=list, + metadata={ + "name": "FiniteVolume", + "type": "Element", + "namespace": "", + }, + ) + + +class SoloEvent(BaseModel): + class Meta: + name = "SoloEvent" + + model_config = ConfigDict(defer_build=True) + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List[PeriodicEvent] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List["SoloEvent"] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_cycle: str = field( + default="-1", + metadata={ + "name": "targetCycle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_timestep: str = field( + default="1", + metadata={ + "name": "targetExactTimestep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_time: str = field( + default="-1", + metadata={ + "name": "targetTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Solvers(BaseModel): + class Meta: + name = "Solvers" + + model_config = ConfigDict(defer_build=True) + acoustic_elastic_sem: List[AcousticElasticSem] = field( + default_factory=list, + metadata={ + "name": "AcousticElasticSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_first_order_sem: List[AcousticFirstOrderSem] = field( + default_factory=list, + metadata={ + "name": "AcousticFirstOrderSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_sem: List[AcousticSem] = field( + default_factory=list, + metadata={ + "name": "AcousticSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_vtisem: List[AcousticVtisem] = field( + default_factory=list, + metadata={ + "name": "AcousticVTISEM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_fvm: List[CompositionalMultiphaseFvm] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseFVM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_hybrid_fvm: List[CompositionalMultiphaseHybridFvm] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseHybridFVM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_reservoir: List[CompositionalMultiphaseReservoir] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoir", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_reservoir_poromechanics: List[ + CompositionalMultiphaseReservoirPoromechanics + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoirPoromechanics", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_well: List[CompositionalMultiphaseWell] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseWell", + "type": "Element", + "namespace": "", + }, + ) + elastic_first_order_sem: List[ElasticFirstOrderSem] = field( + default_factory=list, + metadata={ + "name": "ElasticFirstOrderSEM", + "type": "Element", + "namespace": "", + }, + ) + elastic_sem: List[ElasticSem] = field( + default_factory=list, + metadata={ + "name": "ElasticSEM", + "type": "Element", + "namespace": "", + }, + ) + embedded_surface_generator: List[EmbeddedSurfaceGenerator] = field( + default_factory=list, + metadata={ + "name": "EmbeddedSurfaceGenerator", + "type": "Element", + "namespace": "", + }, + ) + flow_proppant_transport: List[FlowProppantTransport] = field( + default_factory=list, + metadata={ + "name": "FlowProppantTransport", + "type": "Element", + "namespace": "", + }, + ) + hydrofracture: List[Hydrofracture] = field( + default_factory=list, + metadata={ + "name": "Hydrofracture", + "type": "Element", + "namespace": "", + }, + ) + laplace_fem: List[LaplaceFem] = field( + default_factory=list, + metadata={ + "name": "LaplaceFEM", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics: List[MultiphasePoromechanics] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanics", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics_reservoir: List[MultiphasePoromechanicsReservoir] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanicsReservoir", + "type": "Element", + "namespace": "", + }, + ) + phase_field_damage_fem: List[PhaseFieldDamageFem] = field( + default_factory=list, + metadata={ + "name": "PhaseFieldDamageFEM", + "type": "Element", + "namespace": "", + }, + ) + phase_field_fracture: List[PhaseFieldFracture] = field( + default_factory=list, + metadata={ + "name": "PhaseFieldFracture", + "type": "Element", + "namespace": "", + }, + ) + proppant_transport: List[ProppantTransport] = field( + default_factory=list, + metadata={ + "name": "ProppantTransport", + "type": "Element", + "namespace": "", + }, + ) + reactive_compositional_multiphase_obl: List[ReactiveCompositionalMultiphaseObl] = ( + field( + default_factory=list, + metadata={ + "name": "ReactiveCompositionalMultiphaseOBL", + "type": "Element", + "namespace": "", + }, + ) + ) + single_phase_fvm: List[SinglePhaseFvm] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_hybrid_fvm: List[SinglePhaseHybridFvm] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseHybridFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics: List[SinglePhasePoromechanics] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanics", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_conforming_fractures: List[ + SinglePhasePoromechanicsConformingFractures + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsConformingFractures", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_embedded_fractures: List[ + SinglePhasePoromechanicsEmbeddedFractures + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsEmbeddedFractures", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_reservoir: List[SinglePhasePoromechanicsReservoir] = ( + field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsReservoir", + "type": "Element", + "namespace": "", + }, + ) + ) + single_phase_proppant_fvm: List[SinglePhaseProppantFvm] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseProppantFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir: List[SinglePhaseReservoir] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoir", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir_poromechanics: List[SinglePhaseReservoirPoromechanics] = ( + field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoirPoromechanics", + "type": "Element", + "namespace": "", + }, + ) + ) + single_phase_well: List[SinglePhaseWell] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseWell", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_embedded_fractures: List[SolidMechanicsEmbeddedFractures] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsEmbeddedFractures", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrange_contact: List[SolidMechanicsLagrangeContact] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsLagrangeContact", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrangian_ssle: List[SolidMechanicsLagrangianSsle] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsLagrangianSSLE", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrangian_fem: List[SolidMechanicsLagrangianFem] = field( + default_factory=list, + metadata={ + "name": "SolidMechanics_LagrangianFEM", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_mpm: List[SolidMechanicsMpm] = field( + default_factory=list, + metadata={ + "name": "SolidMechanics_MPM", + "type": "Element", + "namespace": "", + }, + ) + surface_generator: List[SurfaceGenerator] = field( + default_factory=list, + metadata={ + "name": "SurfaceGenerator", + "type": "Element", + "namespace": "", + }, + ) + gravity_vector: str = field( + default="{0,0,-9.81}", + metadata={ + "name": "gravityVector", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + + +class Vtkmesh(BaseModel): + class Meta: + name = "VTKMesh" + + model_config = ConfigDict(defer_build=True) + internal_well: List[InternalWell] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + vtkwell: List[Vtkwell] = field( + default_factory=list, + metadata={ + "name": "VTKWell", + "type": "Element", + "namespace": "", + }, + ) + face_blocks: str = field( + default="{}", + metadata={ + "name": "faceBlocks", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + field_names_in_geosx: str = field( + default="{}", + metadata={ + "name": "fieldNamesInGEOSX", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + fields_to_import: str = field( + default="{}", + metadata={ + "name": "fieldsToImport", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + file: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r'.*[\[\]`$].*|[^*?<>\|:";,\s]*\s*', + } + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + main_block_name: str = field( + default="main", + metadata={ + "name": "mainBlockName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + nodeset_names: str = field( + default="{}", + metadata={ + "name": "nodesetNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + partition_method: str = field( + default="parmetis", + metadata={ + "name": "partitionMethod", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|parmetis|ptscotch", + }, + ) + partition_refinement: str = field( + default="1", + metadata={ + "name": "partitionRefinement", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + region_attribute: str = field( + default="attribute", + metadata={ + "name": "regionAttribute", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="{1,1,1}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + surfacic_fields_in_geosx: str = field( + default="{}", + metadata={ + "name": "surfacicFieldsInGEOSX", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + surfacic_fields_to_import: str = field( + default="{}", + metadata={ + "name": "surfacicFieldsToImport", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + translate: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + use_global_ids: str = field( + default="0", + metadata={ + "name": "useGlobalIds", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: str = field( + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + } + ) + + +class Events(BaseModel): + class Meta: + name = "Events" + + model_config = ConfigDict(defer_build=True) + halt_event: List[HaltEvent] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: List[PeriodicEvent] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: List[SoloEvent] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_cycle: str = field( + default="2147483647", + metadata={ + "name": "maxCycle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_time: str = field( + default="1.79769e+308", + metadata={ + "name": "maxTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_time: str = field( + default="0", + metadata={ + "name": "minTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_output_format: str = field( + default="seconds", + metadata={ + "name": "timeOutputFormat", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|seconds|minutes|hours|days|years|full", + }, + ) + + +class Mesh(BaseModel): + class Meta: + name = "Mesh" + + model_config = ConfigDict(defer_build=True) + internal_mesh: List[InternalMesh] = field( + default_factory=list, + metadata={ + "name": "InternalMesh", + "type": "Element", + "namespace": "", + }, + ) + internal_wellbore: List[InternalWellbore] = field( + default_factory=list, + metadata={ + "name": "InternalWellbore", + "type": "Element", + "namespace": "", + }, + ) + particle_mesh: List[ParticleMesh] = field( + default_factory=list, + metadata={ + "name": "ParticleMesh", + "type": "Element", + "namespace": "", + }, + ) + vtkmesh: List[Vtkmesh] = field( + default_factory=list, + metadata={ + "name": "VTKMesh", + "type": "Element", + "namespace": "", + }, + ) + + +class Problem(BaseModel): + class Meta: + name = "Problem" + + model_config = ConfigDict(defer_build=True) + events: List[Events] = field( + default_factory=list, + metadata={ + "name": "Events", + "type": "Element", + "namespace": "", + }, + ) + field_specifications: List[FieldSpecifications] = field( + default_factory=list, + metadata={ + "name": "FieldSpecifications", + "type": "Element", + "namespace": "", + }, + ) + functions: List[Functions] = field( + default_factory=list, + metadata={ + "name": "Functions", + "type": "Element", + "namespace": "", + }, + ) + geometry: List[Geometry] = field( + default_factory=list, + metadata={ + "name": "Geometry", + "type": "Element", + "namespace": "", + }, + ) + mesh: List[Mesh] = field( + default_factory=list, + metadata={ + "name": "Mesh", + "type": "Element", + "namespace": "", + }, + ) + numerical_methods: List[NumericalMethods] = field( + default_factory=list, + metadata={ + "name": "NumericalMethods", + "type": "Element", + "namespace": "", + }, + ) + outputs: List[Outputs] = field( + default_factory=list, + metadata={ + "name": "Outputs", + "type": "Element", + "namespace": "", + }, + ) + solvers: List[Solvers] = field( + default_factory=list, + metadata={ + "name": "Solvers", + "type": "Element", + "namespace": "", + }, + ) + tasks: List[Tasks] = field( + default_factory=list, + metadata={ + "name": "Tasks", + "type": "Element", + "namespace": "", + }, + ) + constitutive: List[Constitutive] = field( + default_factory=list, + metadata={ + "name": "Constitutive", + "type": "Element", + "namespace": "", + }, + ) + element_regions: List[ElementRegions] = field( + default_factory=list, + metadata={ + "name": "ElementRegions", + "type": "Element", + "namespace": "", + }, + ) + particle_regions: List[ParticleRegions] = field( + default_factory=list, + metadata={ + "name": "ParticleRegions", + "type": "Element", + "namespace": "", + }, + ) + included: List[Included] = field( + default_factory=list, + metadata={ + "name": "Included", + "type": "Element", + "namespace": "", + }, + ) + parameters: List[Parameters] = field( + default_factory=list, + metadata={ + "name": "Parameters", + "type": "Element", + "namespace": "", + }, + ) + benchmarks: List[Benchmarks] = field( + default_factory=list, + metadata={ + "name": "Benchmarks", + "type": "Element", + "namespace": "", + }, + ) + + +class Problem(Problem): + pass + model_config = ConfigDict(defer_build=True) diff --git a/geos-trame/src/geos_trame/widgets/__init__.py b/geos-trame/src/geos_trame/widgets/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-trame/src/geos_trame/widgets/geos_trame.py b/geos-trame/src/geos_trame/widgets/geos_trame.py new file mode 100644 index 00000000..758f4a37 --- /dev/null +++ b/geos-trame/src/geos_trame/widgets/geos_trame.py @@ -0,0 +1,17 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from trame_client.widgets.core import AbstractElement + +from .. import module + +__all__ = [ + "Editor", +] + + +class HtmlElement(AbstractElement): + def __init__(self, _elem_name, children=None, **kwargs): + super().__init__(_elem_name, children, **kwargs) + if self.server: + self.server.enable_module(module) diff --git a/geos-trame/tests/__init__.py b/geos-trame/tests/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-trame/tests/conftest.py b/geos-trame/tests/conftest.py new file mode 100644 index 00000000..f4b6d92a --- /dev/null +++ b/geos-trame/tests/conftest.py @@ -0,0 +1,30 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Kitware +import pytest +from pathlib import Path +from trame_client.utils.testing import FixtureHelper + +ROOT_PATH = Path(__file__).parent.parent.absolute() +print(ROOT_PATH) +HELPER = FixtureHelper(ROOT_PATH) + + +@pytest.fixture() +def baseline_image(): + HELPER.remove_page_urls() + yield + HELPER.remove_page_urls() + + +@pytest.fixture +def server(xprocess, server_path): + name, Starter, Monitor = HELPER.get_xprocess_args(server_path) + Starter.timeout = 10 + + # ensure process is running and return its logfile + logfile = xprocess.ensure(name, Starter) + yield Monitor(logfile[1]) + + # clean up whole process tree afterwards + xprocess.getinfo(name).terminate() diff --git a/geos-trame/tests/data/README.md b/geos-trame/tests/data/README.md new file mode 100644 index 00000000..e03aed73 --- /dev/null +++ b/geos-trame/tests/data/README.md @@ -0,0 +1,6 @@ +# Geos data + +All data in this directory comes from the GEOS repository. +As GEOS is under LGPL license, these data are also under LGPL. +The license used by GEOS is here : https://github.com/GEOS-DEV/GEOS/blob/develop/LICENSE + diff --git a/geos-trame/tests/data/singlePhaseFlow/FieldCaseTutorial3_base.xml b/geos-trame/tests/data/singlePhaseFlow/FieldCaseTutorial3_base.xml new file mode 100644 index 00000000..d9efb088 --- /dev/null +++ b/geos-trame/tests/data/singlePhaseFlow/FieldCaseTutorial3_base.xml @@ -0,0 +1,199 @@ + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + diff --git a/geos-trame/tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke.xml b/geos-trame/tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke.xml new file mode 100644 index 00000000..df0089a6 --- /dev/null +++ b/geos-trame/tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke.xml @@ -0,0 +1,27 @@ + + + + + + + + + + + + + + + + + + + + + + diff --git a/geos-trame/tests/data/singlePhaseFlow/synthetic.vtu b/geos-trame/tests/data/singlePhaseFlow/synthetic.vtu new file mode 100644 index 00000000..a0b8bd2b --- /dev/null +++ b/geos-trame/tests/data/singlePhaseFlow/synthetic.vtu @@ -0,0 +1,45 @@ + + + + + + + + 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+5586.944793 +5755.165763 +5923.386732 +6091.607702 +6259.828671 +6428.049641 +6596.270610 +6764.491580 +6932.712549 +7100.933519 +7269.154488 +7437.375458 +7605.596427 +7773.817397 +7942.038366 +8110.259336 +8278.480305 +8446.701275 +8614.922244 +8783.143214 +8951.364183 +9119.585153 +9287.806122 +9456.027092 +9624.248061 +9792.469031 +9960.690000 diff --git a/geos-trame/tests/data/singlePhaseFlow/tables_FieldCaseTuto/zlin.geos b/geos-trame/tests/data/singlePhaseFlow/tables_FieldCaseTuto/zlin.geos new file mode 100644 index 00000000..857f208c --- /dev/null +++ b/geos-trame/tests/data/singlePhaseFlow/tables_FieldCaseTuto/zlin.geos @@ -0,0 +1,10 @@ +1986.480000 +2656.065556 +3325.651111 +3995.236667 +4664.822222 +5334.407778 +6003.993333 +6673.578889 +7343.164444 +8012.750000 diff --git a/geos-trame/tests/requirements.txt b/geos-trame/tests/requirements.txt new file mode 100644 index 00000000..bf9d17bc --- /dev/null +++ b/geos-trame/tests/requirements.txt @@ -0,0 +1,3 @@ +pytest +pytest-seleniumbase +pytest-xprocess diff --git a/geos-trame/tests/test_file_handling.py b/geos-trame/tests/test_file_handling.py new file mode 100644 index 00000000..07fb7462 --- /dev/null +++ b/geos-trame/tests/test_file_handling.py @@ -0,0 +1,17 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Kitware +from trame.app import get_server +from trame_client.utils.testing import enable_testing +from geos_trame.app.core import GeosTrame + + +def test_unsupported_file(capsys): + + server = enable_testing(get_server(client_type="vue3"), "message") + file_name = "tests/data/acous3D/acous3D_vtu.xml" + + GeosTrame(server, file_name) + + captured = capsys.readouterr() + assert captured.err == "Cannot build ui as the input file cannot be parse.\n" diff --git a/geos-trame/tests/test_import.py b/geos-trame/tests/test_import.py new file mode 100644 index 00000000..24f6febe --- /dev/null +++ b/geos-trame/tests/test_import.py @@ -0,0 +1,5 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +def test_import(): + from geos_trame.app.core import GeosTrame # noqa: F401 diff --git a/geos-trame/tests/test_load_and_visualize_synthetic_dataset.py b/geos-trame/tests/test_load_and_visualize_synthetic_dataset.py new file mode 100644 index 00000000..1b26765d --- /dev/null +++ b/geos-trame/tests/test_load_and_visualize_synthetic_dataset.py @@ -0,0 +1,83 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Kitware +import pytest +import os + +from trame.app import get_server +from geos_trame.app.core import GeosTrame + +from seleniumbase import SB +from selenium.webdriver.common.action_chains import ActionChains +from selenium.webdriver.common.by import By + + +@pytest.mark.parametrize("server_path", ["tests/utils/start_geos_trame_for_testing.py"]) +def test_server_state(server): + + # Start geos-trame with a specific xml data + with pytest.raises(Exception): + app = GeosTrame() + + server = get_server() + server.client_type = "vue3" + + file_name = "tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke.xml" + app = GeosTrame(server, file_name) + + # Check that Tree is correctly generated + tree_generated = app.tree.get_tree() + + first_item_is_about_field_specification = "FieldSpecifications" + assert ( + tree_generated["children"][1]["title"] + == first_item_is_about_field_specification + ) + + numerical_methods_node = tree_generated["children"][5] + assert numerical_methods_node["title"] == "NumericalMethods" + finite_volume_node = numerical_methods_node["children"][0] + assert finite_volume_node["title"] == "FiniteVolume" + single_phase_node = finite_volume_node["children"][0] + assert single_phase_node["title"] == "singlePhaseTPFA" + + absolute_mesh_path = app.tree.get_mesh() + parsed_mesh_file_name = os.path.basename(absolute_mesh_path) + expected_mesh_file_name = "synthetic.vtu" + assert parsed_mesh_file_name == expected_mesh_file_name + + +@pytest.mark.parametrize("server_path", ["tests/utils/start_geos_trame_for_testing.py"]) +def test_client_interaction(server, baseline_image): + + with SB(browser="firefox") as sb: + url = f"http://127.0.0.1:{server.port}/" + sb.driver.set_window_size(1848, 1200) + sb.open(url) + sb.sleep(1) + + # Select in the DeckTree the synthetic mesh + sb.driver.find_element(By.ID, "input-76").click() + element = sb.driver.find_element( + By.CSS_SELECTOR, "#v-list-group--id-Problem\\/Mesh\\/0 .mdi-menu-right" + ) + actions = ActionChains(sb.driver) + actions.move_to_element(element).perform() + sb.driver.find_element( + By.CSS_SELECTOR, "#v-list-group--id-Problem\\/Mesh\\/0 .mdi-menu-right" + ).click() + element = sb.driver.find_element(By.CSS_SELECTOR, "body") + actions = ActionChains(sb.driver) + actions.move_to_element(element).perform() + + # Verify that the dataset used is the synthetic.vtu + sb.driver.find_element(By.ID, "input-79").click() + assert sb.get_text("name=Vtkmesh:file:undefined") == "synthetic.vtu" + + # Visualize it in the 3D View: show it and reset the camera + sb.driver.find_element(By.CSS_SELECTOR, ".mdi-eye-off").click() + sb.driver.find_element(By.CSS_SELECTOR, ".mdi-arrow-expand-all").click() + sb.sleep(2) + + # Generate a screenshot + sb.driver.find_element(By.CSS_SELECTOR, ".mdi-file-png-box").click() diff --git a/geos-trame/tests/test_saving_attribute_modification.py b/geos-trame/tests/test_saving_attribute_modification.py new file mode 100644 index 00000000..7f9d438a --- /dev/null +++ b/geos-trame/tests/test_saving_attribute_modification.py @@ -0,0 +1,41 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Kitware +from pathlib import Path +import pytest + +from trame.app import get_server +from geos_trame.app.core import GeosTrame +from trame_client.utils.testing import enable_testing + +from seleniumbase import SB +from selenium.webdriver.common.action_chains import ActionChains +from selenium.webdriver.common.by import By + + +@pytest.mark.parametrize("server_path", ["tests/utils/start_geos_trame_for_testing.py"]) +def test_saving_attribute_modification(server, capsys): + + with SB(browser="firefox") as sb: + url = f"http://127.0.0.1:{server.port}/" + sb.open(url) + sb.sleep(0.5) + + # Modify an attribute of a node + sb.driver.find_element(By.ID, "input-8").click() + sb.driver.find_element(By.NAME, "Events:log_level:undefined").send_keys("25") + + # write the edited file + sb.driver.find_element(By.ID, "save-button").click() + element = sb.driver.find_element(By.CSS_SELECTOR, "body") + actions = ActionChains(sb.driver) + actions.move_to_element(element).perform() + + # Make sure we can load the saved file + server_trame = enable_testing(get_server(client_type="vue3"), "message") + root_path = Path(__file__).parent.absolute().__str__() + file_name = root_path + "tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke_v0.xml" + + GeosTrame(server_trame, file_name) + captured = capsys.readouterr() + assert captured.err == "Cannot build ui as the input file cannot be parse.\n" diff --git a/geos-trame/tests/test_saving_node_modification.py b/geos-trame/tests/test_saving_node_modification.py new file mode 100644 index 00000000..625157d5 --- /dev/null +++ b/geos-trame/tests/test_saving_node_modification.py @@ -0,0 +1,46 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Kitware +from pathlib import Path +import pytest + +from trame.app import get_server +from geos_trame.app.core import GeosTrame +from trame_client.utils.testing import enable_testing + +from seleniumbase import SB +from selenium.webdriver.common.action_chains import ActionChains +from selenium.webdriver.common.by import By + + +@pytest.mark.parametrize("server_path", ["tests/utils/start_geos_trame_for_testing.py"]) +def test_saving_node_modification(server, capsys): + + with SB(browser="firefox") as sb: + url = f"http://127.0.0.1:{server.port}/" + sb.open(url) + sb.sleep(0.5) + + # Modify a node + sb.driver.find_element( + By.CSS_SELECTOR, "#v-list-group--id-Problem\\/Events\\/0 .mdi-menu-right" + ).click() + sb.driver.find_element(By.ID, "input-14").click() + sb.driver.find_element(By.NAME, "PeriodicEvent:begin_time:undefined").send_keys( + "19" + ) + + # write the edited file + sb.driver.find_element(By.ID, "save-button").click() + element = sb.driver.find_element(By.CSS_SELECTOR, "body") + actions = ActionChains(sb.driver) + actions.move_to_element(element).perform() + + # Make sure we can load the saved file + server_trame = enable_testing(get_server(client_type="vue3"), "message") + root_path = Path(__file__).parent.absolute().__str__() + file_name = root_path + "tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke_v0.xml" + + GeosTrame(server_trame, file_name) + captured = capsys.readouterr() + assert captured.err == "Cannot build ui as the input file cannot be parse.\n" diff --git a/geos-trame/tests/test_saving_subnode_modifications.py b/geos-trame/tests/test_saving_subnode_modifications.py new file mode 100644 index 00000000..02e4adc4 --- /dev/null +++ b/geos-trame/tests/test_saving_subnode_modifications.py @@ -0,0 +1,59 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Kitware +from pathlib import Path +import pytest + +from trame.app import get_server +from geos_trame.app.core import GeosTrame +from trame_client.utils.testing import enable_testing + +from seleniumbase import SB +from selenium.webdriver.common.action_chains import ActionChains +from selenium.webdriver.common.by import By + + +@pytest.mark.parametrize("server_path", ["tests/utils/start_geos_trame_for_testing.py"]) +def test_saving_subnode_modifications(server, capsys): + + with SB(browser="firefox") as sb: + url = f"http://127.0.0.1:{server.port}/" + sb.open(url) + sb.sleep(0.5) + + # Modify a subnode + sb.driver.find_element( + By.CSS_SELECTOR, + "#v-list-group--id-Problem\\/NumericalMethods\\/0 .mdi-menu-right", + ).click() + element = sb.driver.find_element(By.CSS_SELECTOR, "body") + element = sb.driver.find_element( + By.CSS_SELECTOR, + "#v-list-group--id-Problem\\/NumericalMethods\\/0\\/FiniteVolume\\/0 .mdi-menu-right", + ) + sb.driver.find_element( + By.CSS_SELECTOR, + "#v-list-group--id-Problem\\/NumericalMethods\\/0\\/FiniteVolume\\/0 .mdi-menu-right", + ).click() + element = sb.driver.find_element(By.CSS_SELECTOR, "body") + sb.driver.find_element(By.ID, "input-93").click() + + element = sb.driver.find_element(By.CSS_SELECTOR, ".mdi-content-save-outline") + sb.driver.find_element( + By.NAME, "TwoPointFluxApproximation:upwinding_scheme:undefined" + ).send_keys("PPA") + + # write the edited file + sb.driver.find_element(By.ID, "save-button").click() + element = sb.driver.find_element(By.CSS_SELECTOR, "body") + actions = ActionChains(sb.driver) + actions.move_to_element(element).perform() + + # Make sure we can load the saved file + server_trame = enable_testing(get_server(client_type="vue3"), "message") + root_path = Path(__file__).parent.absolute().__str__() + file_name = root_path + "tests/data/singlePhaseFlow/FieldCaseTutorial3_smoke_v0.xml" + + GeosTrame(server_trame, file_name) + captured = capsys.readouterr() + assert captured.err == "Cannot build ui as the input file cannot be parse.\n" diff --git a/geos-trame/tests/utils/__init__.py b/geos-trame/tests/utils/__init__.py new file mode 100644 index 00000000..e69de29b diff --git a/geos-trame/tests/utils/start_geos_trame_for_testing.py b/geos-trame/tests/utils/start_geos_trame_for_testing.py new file mode 100644 index 00000000..e3b033ac --- /dev/null +++ b/geos-trame/tests/utils/start_geos_trame_for_testing.py @@ -0,0 +1,15 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from trame_client.utils.testing import enable_testing +from geos_trame.app.core import GeosTrame +from trame.app import get_server +from pathlib import Path + +root_path = Path(__file__).parent.parent.absolute().__str__() +file_name = root_path + "/data/singlePhaseFlow/FieldCaseTutorial3_smoke.xml" + +server = enable_testing(get_server(client_type="vue3"), "message") +app = GeosTrame(server, file_name) + +app.server.start() diff --git a/geos-trame/tests/utils/testing_tools.py b/geos-trame/tests/utils/testing_tools.py new file mode 100644 index 00000000..37df8981 --- /dev/null +++ b/geos-trame/tests/utils/testing_tools.py @@ -0,0 +1,24 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from PIL import Image +from PIL import ImageChops + + +def image_pixel_differences(base_image_path, compare_image_path): + """ + Calculates the bounding box of the non-zero regions in the image. + :param base_image: target image to find + :param compare_image: set of images containing the target image + :return: True is the L1 value between each image is identitic, + False otherwise + """ + + base_image = Image.open(base_image_path) + compare_image = Image.open(compare_image_path) + + diff = ImageChops.difference(base_image, compare_image) + if diff.getbbox(): + return False + else: + return True diff --git a/geos-trame/vue-components/.editorconfig b/geos-trame/vue-components/.editorconfig new file mode 100644 index 00000000..9d08a1a8 --- /dev/null +++ b/geos-trame/vue-components/.editorconfig @@ -0,0 +1,9 @@ +root = true + +[*] +charset = utf-8 +indent_style = space +indent_size = 2 +end_of_line = lf +insert_final_newline = true +trim_trailing_whitespace = true diff --git a/geos-trame/vue-components/.eslintrc.cjs b/geos-trame/vue-components/.eslintrc.cjs new file mode 100644 index 00000000..dba6d34e --- /dev/null +++ b/geos-trame/vue-components/.eslintrc.cjs @@ -0,0 +1,14 @@ +/* eslint-env node */ +require("@rushstack/eslint-patch/modern-module-resolution"); + +module.exports = { + root: true, + extends: [ + "plugin:vue/vue3-essential", + "eslint:recommended", + "@vue/eslint-config-prettier", + ], + parserOptions: { + ecmaVersion: "latest", + }, +}; diff --git a/geos-trame/vue-components/.gitignore b/geos-trame/vue-components/.gitignore new file mode 100644 index 00000000..64debff0 --- /dev/null +++ b/geos-trame/vue-components/.gitignore @@ -0,0 +1,29 @@ +# Logs +logs +*.log +npm-debug.log* +yarn-debug.log* +yarn-error.log* +pnpm-debug.log* +lerna-debug.log* + +node_modules +.DS_Store +dist +dist-ssr +coverage +*.local + +/cypress/videos/ +/cypress/screenshots/ + +# Editor directories and files +.vscode/* 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.gitignore --ignore-pattern public", + "semantic-release": "semantic-release" + }, + "dependencies": { + }, + "peerDependencies": { + "vue": "^2.7.0 || >=3.0.0" + }, + "devDependencies": { + "@rushstack/eslint-patch": "^1.1.4", + "@vue/eslint-config-prettier": "^7.0.0", + "eslint": "^8.33.0", + "eslint-plugin-vue": "^9.3.0", + "prettier": "^2.7.1", + "semantic-release": "19.0.2", + "vite": "^4.1.0", + "vue": "^3.0.0" + }, + "files": [ + "dist/*", + "src/*", + "*.json", + "*.js" + ] +} diff --git a/geos-trame/vue-components/src/components/CustomWidget.js b/geos-trame/vue-components/src/components/CustomWidget.js new file mode 100644 index 00000000..4addf26f --- /dev/null +++ b/geos-trame/vue-components/src/components/CustomWidget.js @@ -0,0 +1,30 @@ +export default { + emits: ["click", "change"], + props: { + attribute_name: { + type: String, + }, + js_attr_name: { + type: String, + }, + }, + setup(props, { emit }) { + const btnClick = "margin: 0 10px;background: #F48FB1 !important;"; + const btnChange = "margin: 0 10px;#CE93D8 !important;"; + const triggerClick = () => emit("click"); + const triggerChange = () => emit("change"); + + return { + btnClick, + btnChange, + triggerClick, + triggerChange, + }; + }, + template: ` +
+ Custom click + Custom change +
`, + }; + \ No newline at end of file diff --git a/geos-trame/vue-components/src/components/index.js b/geos-trame/vue-components/src/components/index.js new file mode 100644 index 00000000..890580b2 --- /dev/null +++ b/geos-trame/vue-components/src/components/index.js @@ -0,0 +1,5 @@ +import CustomWidget from './CustomWidget'; + +export default { + 'yourCustomWidget':CustomWidget, +}; diff --git a/geos-trame/vue-components/src/main.js b/geos-trame/vue-components/src/main.js new file mode 100644 index 00000000..55d953f7 --- /dev/null +++ b/geos-trame/vue-components/src/main.js @@ -0,0 +1,7 @@ +import components from "./components"; + +export function install(Vue) { + Object.keys(components).forEach((name) => { + Vue.component(name, components[name]); + }); +} diff --git a/geos-trame/vue-components/vite.config.js b/geos-trame/vue-components/vite.config.js new file mode 100644 index 00000000..e66ebfe0 --- /dev/null +++ b/geos-trame/vue-components/vite.config.js @@ -0,0 +1,21 @@ +export default { + base: "./", + build: { + lib: { + entry: "./src/main.js", + name: "geos_trame", + formats: ["umd"], + fileName: "geos_trame", + }, + rollupOptions: { + external: ["vue"], + output: { + globals: { + vue: "Vue", + }, + }, + }, + outDir: "../src/geos_trame/module/serve", + assetsDir: ".", + }, +}; diff --git a/geos-xml-viewer/.gitignore b/geos-xml-viewer/.gitignore new file mode 100644 index 00000000..68bc17f9 --- /dev/null +++ b/geos-xml-viewer/.gitignore @@ -0,0 +1,160 @@ +# Byte-compiled / optimized / DLL files +__pycache__/ +*.py[cod] +*$py.class + +# C extensions +*.so + +# Distribution / packaging +.Python +build/ +develop-eggs/ +dist/ +downloads/ +eggs/ +.eggs/ +lib/ +lib64/ +parts/ +sdist/ +var/ +wheels/ +share/python-wheels/ +*.egg-info/ +.installed.cfg +*.egg +MANIFEST + +# PyInstaller +# Usually these files are written by a python script from a template +# before PyInstaller builds the exe, so as to inject date/other infos into it. +*.manifest +*.spec + +# Installer logs +pip-log.txt +pip-delete-this-directory.txt + +# Unit test / coverage reports +htmlcov/ +.tox/ +.nox/ +.coverage +.coverage.* +.cache +nosetests.xml +coverage.xml +*.cover +*.py,cover +.hypothesis/ +.pytest_cache/ +cover/ + +# Translations +*.mo +*.pot + +# Django stuff: +*.log +local_settings.py +db.sqlite3 +db.sqlite3-journal + +# Flask stuff: +instance/ +.webassets-cache + +# Scrapy stuff: +.scrapy + +# Sphinx documentation +docs/_build/ + +# PyBuilder +.pybuilder/ +target/ + +# Jupyter Notebook +.ipynb_checkpoints + +# IPython +profile_default/ +ipython_config.py + +# pyenv +# For a library or package, you might want to ignore these files since the code is +# intended to run in multiple environments; otherwise, check them in: +# .python-version + +# pipenv +# According to pypa/pipenv#598, it is recommended to include Pipfile.lock in version control. +# However, in case of collaboration, if having platform-specific dependencies or dependencies +# having no cross-platform support, pipenv may install dependencies that don't work, or not +# install all needed dependencies. +#Pipfile.lock + +# poetry +# Similar to Pipfile.lock, it is generally recommended to include poetry.lock in version control. +# This is especially recommended for binary packages to ensure reproducibility, and is more +# commonly ignored for libraries. +# https://python-poetry.org/docs/basic-usage/#commit-your-poetrylock-file-to-version-control +#poetry.lock + +# pdm +# Similar to Pipfile.lock, it is generally recommended to include pdm.lock in version control. +#pdm.lock +# pdm stores project-wide configurations in .pdm.toml, but it is recommended to not include it +# in version control. +# https://pdm.fming.dev/#use-with-ide +.pdm.toml + +# PEP 582; used by e.g. github.com/David-OConnor/pyflow and github.com/pdm-project/pdm +__pypackages__/ + +# Celery stuff +celerybeat-schedule +celerybeat.pid + +# SageMath parsed files +*.sage.py + +# Environments +.env +.venv +env/ +venv/ +ENV/ +env.bak/ +venv.bak/ + +# Spyder project settings +.spyderproject +.spyproject + +# Rope project settings +.ropeproject + +# mkdocs documentation +/site + +# mypy +.mypy_cache/ +.dmypy.json +dmypy.json + +# Pyre type checker +.pyre/ + +# pytype static type analyzer +.pytype/ + +# Cython debug symbols +cython_debug/ + +# PyCharm +# JetBrains specific template is maintained in a separate JetBrains.gitignore that can +# be found at https://github.com/github/gitignore/blob/main/Global/JetBrains.gitignore +# and can be added to the global gitignore or merged into this file. For a more nuclear +# option (not recommended) you can uncomment the following to ignore the entire idea folder. +#.idea/ diff --git a/geos-xml-viewer/README.md b/geos-xml-viewer/README.md new file mode 100644 index 00000000..c9954553 --- /dev/null +++ b/geos-xml-viewer/README.md @@ -0,0 +1,18 @@ + +# Geos Xml Viewer + + +## Welcome +geos-xml-viewer is a Python package dedicated visualize data from geos simulation xml input file. + +## Overview + +This package provides the following main functionalities: + + - export data from deck and vtu file to a PartitionedDataSetCollection + - deck object (mesh, wells, boxes) visualization + - split a deck into multiple files (e.g. one per main node) diff --git a/geos-xml-viewer/pyproject.toml b/geos-xml-viewer/pyproject.toml new file mode 100644 index 00000000..ea554f21 --- /dev/null +++ b/geos-xml-viewer/pyproject.toml @@ -0,0 +1,181 @@ +[build-system] +requires = ["setuptools>=61.2"] +build-backend = "setuptools.build_meta" + +[tool.setuptools] +include-package-data = true + +[tool.setuptools.packages.find] +where = ["src"] +include = ["geos_xml_viewer*", "PVplugins*"] +exclude = ['tests*'] + +[project] +name = "geos-xml-viewer" +version = "1.2.1" +description = "geos-xml-viewer is a Python package dedicated to preprocessing and postpressing of data for the geos simulation framework" +authors = [{name = "Lionel Untereiner", email = "lionel.untereiner@external.totalenergies.com"}] +license = {text = "Apache-2.0"} +classifiers = [ + "Programming Language :: Python :: 3", + "Development Status :: 4 - Beta", + "Intended Audience :: Developers", + "Intended Audience :: Science/Research", + "License :: OSI Approved :: Apache Software License ", + "Natural Language :: English", + "Operating System :: POSIX :: Linux", + "Operating System :: MacOS :: MacOS X", + "Topic :: Scientific/Engineering :: Visualization", +] +keywords = [ + "GEOS", + "Simulation", +] +readme = {file = "README.md", content-type = "text/markdown"} +dependencies = [ + "pyvista >= 0.42", + "lxml >= 4.9", + "xsdata >= 24", + "colorcet >= 3.0.1", +] +requires-python = ">= 3.9" + +[project.urls] +Homepage = "https://github.com/GEOS-DEV/geosPythonPackages" +Documentation = "https://geosx-geosx.readthedocs-hosted.com/projects/geosx-geospythonpackages/en/latest/" +Repository = "https://github.com/GEOS-DEV/geosPythonPackages.git" +"Bug Tracker" = "https://github.com/GEOS-DEV/geosPythonPackages/issues" + +[project.optional-dependencies] +cli = ["xsdata[cli]>=24"] +build = [ + "build >= 1.2" +] +dev = [ + "pylint", + "mypy", + "ruff", + "black", + "xmlschema" +] +test = [ + "coverage", + "pytest" +] + +[project.scripts] +geos-viewer = "geos_xml_viewer.bin.viewer:run" +geos-exporter = "geos_xml_viewer.bin.exporter:run" +#validate = "geos_xml_viewer.bin.validate:run" +#xsd = "geos_xml_viewer.bin.test_xsdata:run" +geos-modifier = "geos_xml_viewer.bin.modifier:run" +#testCellLocator = "geos_xml_viewer.bin.testCellLocator:run" +geos-splitter = "geos_xml_viewer.bin.splitter:run" + +[tool.bumpversion] +current_version = "1.2.1" + +[[tool.bumpversion.files]] +filename = "pyproject.toml" +search = 'version = "{current_version}"' + +[tool.ruff] +target-version = "py39" + +[tool.ruff.lint] +select = [ + "E", # pycodestyle errors + "W", # pycodestyle warnings + "F", # pyflakes + "UP", # pyupgrade + "B", # flake8-bugbear + "SIM", # flake8-simplify + "ANN", # flake8-annotations + "C4", # flake8-comprehensions + "I", # isort + "D", # pydocstyle +] + +ignore = [ + "E501", # line too long, handled by black + "B008", # do not perform function calls in argument defaults + "C901", # too complex + "W191", # indentation contains tabs + "D100", + "D101", + "D104", # Missing docstring in public package in __init__.py files + "UP007", +] + +[tool.ruff.lint.isort] +known-third-party = ["pyvista"] + +[tool.ruff.lint.pyupgrade] +# Preserve types, even if a file imports `from __future__ import annotations`. +keep-runtime-typing = true + +[tool.ruff.lint.pydocstyle] +convention = "google" + +# [tool.black] +# line-length = 88 +# target-version = ["py39", "py310", "py311"] +# include = '\.pyi?$' +# exclude = ''' +# /( +# \.git +# | \.hg +# | \.mypy_cache +# | \.pytest_cache +# | \.tox +# | \.venv +# | _build +# | buck-out +# | build +# | dist +# | htmlcov +# )/ +# ''' + +# [tool.isort] +# multi_line_output = 3 +# atomic = true +# profile = "black" +# line_length = 88 +# skip_gitignore = true +# include_trailing_comma = true +# # skip_glob = ["tests"] + +[tool.pytest.ini_options] +addopts = [ + "--import-mode=importlib", +] +console_output_style = "count" +python_classes = "Test" +python_files = "test_*.py" +python_functions = "test*" +testpaths = ["tests"] +pythonpath = [ + "src", +] + +[tool.coverage.run] +branch = true +source = ["src"] + + +[tool.mypy] +# Specify the target platform details in config, so your developers are +# free to run mypy on Windows, Linux, or macOS and get consistent +# results. +python_version = "3.9" +mypy_path = "src" +strict = true +# Unreachable blocks have been an issue when compiling mypyc, let's try to avoid 'em in the first place. +warn_unreachable = true +implicit_reexport = true +show_error_codes = true +show_column_numbers = true +exclude = [ + 'geos_xml_viewer/algorithms/write_wells.py', +] \ No newline at end of file diff --git a/geos-xml-viewer/src/PVplugins/__init__.py b/geos-xml-viewer/src/PVplugins/__init__.py new file mode 100644 index 00000000..ffa33702 --- /dev/null +++ b/geos-xml-viewer/src/PVplugins/__init__.py @@ -0,0 +1,4 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + diff --git a/geos-xml-viewer/src/PVplugins/deckReader.py b/geos-xml-viewer/src/PVplugins/deckReader.py new file mode 100644 index 00000000..446be089 --- /dev/null +++ b/geos-xml-viewer/src/PVplugins/deckReader.py @@ -0,0 +1,73 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from typing import Self + +from paraview.util.vtkAlgorithm import smdomain, smhint, smproperty, smproxy +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase +from vtkmodules.vtkCommonCore import vtkInformation, vtkInformationVector +from vtkmodules.vtkCommonDataModel import vtkPartitionedDataSetCollection + +paraview_plugin_version = "0.1.0" + + +@smproxy.reader( + name="PythonGeosDeckReader", + label="Python-based Deck Reader for GEOS", + extensions="xml", + file_description="XML files", +) +class PVGeosDeckReader(VTKPythonAlgorithmBase): + def __init__(self: Self) -> Self: + """Constructor of the reader.""" + VTKPythonAlgorithmBase.__init__( + self, + nInputPorts=0, + nOutputPorts=1, + outputType="vtkPartitionedDataSetCollection", + ) # type: ignore + self.__filename: str + from geos_xml_viewer.filters.geosDeckReader import GeosDeckReader + + self.__realAlgorithm = GeosDeckReader() + + @smproperty.stringvector(name="FileName") # type: ignore + @smdomain.filelist() # type: ignore + @smhint.filechooser(extensions="xml", file_description="GEOS XML files") # type: ignore + def SetFileName(self: Self, name: str) -> None: + """Specify filename for the file to read. + + Args: + name (str): filename + """ + if self.__filename != name: + self.__filename = name + self.__realAlgorithm.SetFileName(self.__filename) + self.__realAlgorithm.Update() + self.Modified() + + def RequestData( + self: Self, + request: vtkInformation, + inInfoVec: list[vtkInformationVector], + outInfoVec: vtkInformationVector, + ) -> int: + """RequestData function of the vtk pipeline. + + Args: + request (vtkInformation): information about the request + inInfoVec (list[vtkInformationVector]): input information vector + outInfoVec (vtkInformationVector): output information vector + + Raises: + RuntimeError: Raises an error if no filename is specified + + Returns: + int: Returns 1 if the pipeline is successful + """ + if self.__filename is None: + raise RuntimeError("No filename specified") + + output = vtkPartitionedDataSetCollection.GetData(inInfoVec, 0) + output.ShallowCopy(self.__realAlgorithm.GetOutputDataObject(0)) + return 1 diff --git a/geos-xml-viewer/src/PVplugins/geostkParaviewPlugin.py b/geos-xml-viewer/src/PVplugins/geostkParaviewPlugin.py new file mode 100644 index 00000000..6d35f920 --- /dev/null +++ b/geos-xml-viewer/src/PVplugins/geostkParaviewPlugin.py @@ -0,0 +1,8 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import os +import sys + +sys.path.append(os.path.dirname(__file__)) diff --git a/geos-xml-viewer/src/PVplugins/py.typed b/geos-xml-viewer/src/PVplugins/py.typed new file mode 100644 index 00000000..e69de29b diff --git a/geos-xml-viewer/src/geos_xml_viewer/__init__.py b/geos-xml-viewer/src/geos_xml_viewer/__init__.py new file mode 100644 index 00000000..eb6e016e --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/__init__.py @@ -0,0 +1,6 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + + +__version__ = "0.1.0" diff --git a/geos-xml-viewer/src/geos_xml_viewer/algorithms/__init__.py b/geos-xml-viewer/src/geos_xml_viewer/algorithms/__init__.py new file mode 100644 index 00000000..32657d78 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/algorithms/__init__.py @@ -0,0 +1,6 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + + +# only imports certain functions from library diff --git a/geos-xml-viewer/src/geos_xml_viewer/algorithms/deck.py b/geos-xml-viewer/src/geos_xml_viewer/algorithms/deck.py new file mode 100644 index 00000000..ca75ea5a --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/algorithms/deck.py @@ -0,0 +1,974 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import re +from typing import NamedTuple, List, Any, TextIO +from ast import literal_eval +from enum import IntEnum +from os.path import expandvars +from pathlib import Path +import io + +import numpy as np +import numpy.typing as npt +import vtk # type: ignore[import-untyped] +from lxml import etree as ElementTree # type: ignore[import-untyped] +from lxml.etree import XMLSyntaxError # type: ignore[import-untyped] +from vtk.util.numpy_support import numpy_to_vtk as numpy_to_vtk_ + +tr = str.maketrans("{}", "[]") + +CLASS_READERS = { + # Standard dataset readers: + ".pvti": vtk.vtkXMLPImageDataReader, + ".pvtr": vtk.vtkXMLPRectilinearGridReader, + ".pvtu": vtk.vtkXMLPUnstructuredGridReader, + ".vti": vtk.vtkXMLImageDataReader, + ".vtp": vtk.vtkXMLPolyDataReader, + ".vtr": vtk.vtkXMLRectilinearGridReader, + ".vts": vtk.vtkXMLStructuredGridReader, + ".vtu": vtk.vtkXMLUnstructuredGridReader, +} + +COMPOSITE_DATA_READERS = { + ".vtm": vtk.vtkXMLMultiBlockDataReader, + ".vtmb": vtk.vtkXMLMultiBlockDataReader, +} + +class SimulationDeck(NamedTuple): + file_path: str + xml_root: ElementTree.Element + + +class TreeViewNodeType(IntEnum): + UNKNOWN = 1 + REPRESENTATION = 2 + PROPERTIES = 3 + WELLBORETRAJECTORY = 4 + WELLBOREFRAME = 5 + WELLBORECHANNEL = 6 + WELLBOREMARKER = 7 + WELLBORECOMPLETION = 8 + TIMESERIES = 9 + PERFORATION = 10 + + +def numpy_to_vtk(a: npt.DTypeLike) -> vtk.vtkDataArray: + return numpy_to_vtk_(a, deep=1) # , array_type=get_vtk_array_type(a.dtype)) + + +# def getBlockNameAndLabel(metadata: vtk.vtkInformation, defaultName: str) -> [str, str]: +# if ( +# metadata is not None +# and metadata.Has(vtk.vtkCompositeDataSet.NAME()) +# and metadata.Get(vtk.vtkCompositeDataSe.NAME()) +# ): +# label: str = metadata.Get(vtk.vtkCompositeDataSet.NAME()) +# if not label.empty(): +# name: str = vtk.vtkDataAssembly.MakeValidNodeName(label) +# return [name, label] + +# return [defaultName, ""] + + +def read(xmlFilepath: str) -> SimulationDeck: + """Reads an xml file (and recursively its included files) into memory + + Args: + xmlFilepath (str): The path the file to read. + + Returns: + SimulationDeck: The simulation deck + """ + expanded_file = Path(expandvars(xmlFilepath)).expanduser().resolve() + file_path = expanded_file.parent + + try: + parser = ElementTree.XMLParser(remove_comments=True, remove_blank_text=True) + tree = ElementTree.parse(expanded_file, parser=parser) + root = tree.getroot() + except XMLSyntaxError as err: + print("\nCould not load input file: %s" % (expanded_file)) + print(err.msg) + raise Exception("\nCheck input file!") from err + + includeCount = 0 + for include_node in root.findall("Included"): + for f in include_node.findall("File"): + _merge_included_xml_files(root, file_path, f.get("name"), includeCount) + + # Remove 'Included' nodes + for include_node in root.findall("Included"): + root.remove(include_node) + + for neighbor in root.iter(): + for key in neighbor.attrib.keys(): + s = re.sub(r"\s{2,}", " ", neighbor.get(key)) + neighbor.set(key, s) + + return SimulationDeck(file_path, root) + + +def build_model( + d: SimulationDeck, collection: vtk.vtkPartitionedDataSetCollection, attr: str +) -> int: + """_summary_ + + Args: + d (SimulationDeck): _description_ + collection (vtk.vtkPartitionedDataSetCollection): _description_ + attr (str): _description_ + + Returns: + _type_: _description_ + """ + assembly = vtk.vtkDataAssembly() + # FIXME could be deck name + assembly.SetRootNodeName(Path(d.file_path).stem) + collection.SetDataAssembly(assembly) + + # Step 1 - mesh + # read the mesh as first child of root node + if _read_mesh(d, collection, attr) < 0: + return 0 + + # Step 2 - wells + if _read_wells(d, collection) < 0: + return 0 + + # Step 3 - boxes + if _read_boxes(d, collection) < 0: + return 0 + + return 1 + +def _read_boxes( + d: SimulationDeck, collection: vtk.vtkPartitionedDataSetCollection +) -> int: + geometric_objects = d.xml_root.find("Geometry") + + if geometric_objects is None: + return 0 + + boxes = geometric_objects.findall("Box") + + if not boxes: + return 0 + + count: int = collection.GetNumberOfPartitionedDataSets() + + assembly = collection.GetDataAssembly() + node = assembly.AddNode("Boxes") + + for idx, box in enumerate(boxes): + p = vtk.vtkPartitionedDataSet() + # geometry + xmin = box.attrib["xMin"] + xmin_array = np.array(literal_eval(xmin.translate(tr)), dtype=np.float64) + xmax = box.attrib["xMax"] + xmax_array = np.array(literal_eval(xmax.translate(tr)), dtype=np.float64) + + bounds = ( + xmin_array[0], + xmax_array[0], + xmin_array[1], + xmax_array[1], + xmin_array[2], + xmax_array[2], + ) + + box = vtk.vtkTessellatedBoxSource() + box.SetBounds(bounds) + box.Update() + b = box.GetOutput() + + p.SetPartition(0, b) + + collection.SetPartitionedDataSet(count, p) + collection.GetMetaData(count).Set( + vtk.vtkCompositeDataSet.NAME(), "Box" + str(idx) + ) + + idbox = assembly.AddNode("Box", node) + assembly.SetAttribute(idbox, "label", "Box" + str(idx)) + assembly.SetAttribute(idbox, "type", TreeViewNodeType.REPRESENTATION) + assembly.SetAttribute( + idbox, "number_of_partitions", collection.GetNumberOfPartitions(count) + ) + assembly.AddDataSetIndex(idbox, count) + count = count + 1 + + return 1 + +def _read_wells( + d: SimulationDeck, collection: vtk.vtkPartitionedDataSetCollection +) -> int: + meshes = d.xml_root.find("Mesh") + + if meshes is None: + raise Exception("\nMesh node not found") + + wells = meshes.findall(".//InternalWell") + + if not wells: + return 0 + + count: int = collection.GetNumberOfPartitionedDataSets() + + assembly = collection.GetDataAssembly() + node = assembly.AddNode("Wells") + + for idx, well in enumerate(wells): + # geometry + s = well.attrib["polylineNodeCoords"] + points = np.array(literal_eval(s.translate(tr)), dtype=np.float64) + tip = points[0] + + # combinatorics + s = well.attrib["polylineSegmentConn"] + lines = np.array(literal_eval(s.translate(tr)), dtype=np.int64) + v_indices = np.unique(lines.flatten()) + + r = literal_eval(well.attrib["radius"].translate(tr)) + radius = np.repeat(r, points.shape[0]) + + vpoints = vtk.vtkPoints() + vpoints.SetNumberOfPoints(points.shape[0]) + vpoints.SetData(numpy_to_vtk(points)) + + polyLine = vtk.vtkPolyLine() + polyLine.GetPointIds().SetNumberOfIds(len(v_indices)) + + for iline, vidx in enumerate(v_indices): + polyLine.GetPointIds().SetId(iline, vidx) + + cells = vtk.vtkCellArray() + cells.InsertNextCell(polyLine) + + vradius = vtk.vtkDoubleArray() + vradius.SetName("radius") + vradius.SetNumberOfComponents(1) + vradius.SetNumberOfTuples(points.shape[0]) + vradius.SetVoidArray(numpy_to_vtk(radius), points.shape[0], 1) + + polyData = vtk.vtkPolyData() + polyData.SetPoints(vpoints) + polyData.SetLines(cells) + polyData.GetPointData().AddArray(vradius) + polyData.GetPointData().SetActiveScalars("radius") + + p = vtk.vtkPartitionedDataSet() + p.SetPartition(0, polyData) + collection.SetPartitionedDataSet(count, p) + + collection.GetMetaData(count).Set( + vtk.vtkCompositeDataSet.NAME(), + well.attrib["name"], + ) + + idwell = assembly.AddNode("Well", node) + assembly.SetAttribute(idwell, "label", well.attrib["name"]) + + well_mesh_node = assembly.AddNode("Mesh", idwell) + assembly.SetAttribute(well_mesh_node, "type", TreeViewNodeType.REPRESENTATION) + assembly.SetAttribute( + well_mesh_node, + "number_of_partitions", + collection.GetNumberOfPartitions(count), + ) + assembly.AddDataSetIndex(well_mesh_node, count) + count = count + 1 + + perforations = well.findall("Perforation") + perf_node = assembly.AddNode("Perforations", idwell) + assembly.SetAttribute(perf_node, "label", "Perforations") + for idxp, perfo in enumerate(perforations): + pp = vtk.vtkPartitionedDataSet() + name = perfo.attrib["name"] + z = literal_eval(perfo.attrib["distanceFromHead"].translate(tr)) + + ppoints = vtk.vtkPoints() + ppoints.SetNumberOfPoints(1) + perfo_point = np.array([tip[0], tip[1], tip[2] - z], dtype=np.float64) + ppoints.SetPoint(0, perfo_point) + + polyData = vtk.vtkPolyData() + polyData.SetPoints(ppoints) + + pp.SetPartition(0, polyData) + collection.SetPartitionedDataSet(count, pp) + collection.GetMetaData(count).Set( + vtk.vtkCompositeDataSet.NAME(), + name, + ) + + idperf = assembly.AddNode("Perforation", perf_node) + assembly.SetAttribute(idperf, "label", name) + assembly.SetAttribute(idperf, "type", TreeViewNodeType.REPRESENTATION) + assembly.AddDataSetIndex(idperf, count) + count = count + 1 + + return 1 + +def _read_mesh( + d: SimulationDeck, + collection: vtk.vtkPartitionedDataSetCollection, + attr: str, +) -> int: + """Reads the mesh from the simulation deck + + Args: + d (SimulationDeck): _description_ + collection (vtk.vtkPartitionedDataSetCollection): _description_ + + Raises: + Exception: _description_ + Exception: _description_ + + Returns: + vtk.vtkPartitionedDataSet: the mesh as a partition of the data from the deck + """ + meshes = d.xml_root.find("Mesh") + + if meshes is None: + raise Exception("\nMesh node not found") + + mesh = meshes.find("VTKMesh") + if mesh is not None: + if _read_vtk_data_repository(d.file_path, mesh, collection, attr) < 1: + return 0 + + mesh = meshes.find("InternalMesh") + if mesh is not None: + _generate_grid(mesh, collection) + + + return 1 + # else: + # raise Exception("\nNeither VTKMesh or InternalMesh node were found") + +def _read_vtk_data_repository( + file_path: str, + mesh: ElementTree.Element, + collection: vtk.vtkPartitionedDataSetCollection, + attr: str, +) -> int: + """Reads the mesh added in the simulation deck and builds adds it as a partition + + Args: + file_path (str): Path where the mesh is + mesh (ElementTree.Element): XML node of the mesh + collection (vtk.vtkPartitionedDataSetCollection): Current collection to update + attr (str): Cell attribute name to use as region marker + + Returns: + int: Updated global dataset index + """ + path = Path(file_path) / mesh.attrib["file"] + + count: int = collection.GetNumberOfPartitionedDataSets() + assembly = collection.GetDataAssembly() + + id_mesh = assembly.AddNode("Mesh") + assembly.SetAttribute(id_mesh, "label", mesh.attrib["name"]) + assembly.SetAttribute(id_mesh, "type", TreeViewNodeType.REPRESENTATION) + + id_surf = assembly.AddNode("Surfaces") + + if path.suffix in CLASS_READERS: + try: + Reader = CLASS_READERS[path.suffix] + except KeyError as err: + # raise ValueError( + # f"`read` does not support a file with the {path.suffix} extension" + # ) from err + + return 0 + + reader = Reader() + reader.SetFileName(path) + reader.Update() + + ugrid: vtk.vtkUnstructuredGrid = reader.GetOutputDataObject(0) # use pv.wrap() + + attr_array = ugrid.GetCellData().GetArray(attr) + [attr_min, attr_max] = attr_array.GetRange() + + # load surfaces + for i in range(int(attr_min), int(attr_max + 1)): + threshold = vtk.vtkThreshold() + threshold.SetInputData(ugrid) + threshold.SetUpperThreshold(i) + threshold.SetLowerThreshold(i) + threshold.SetInputArrayToProcess( + 0, 0, 0, vtk.vtkDataObject.FIELD_ASSOCIATION_CELLS, attr + ) + + extract = vtk.vtkExtractCellsByType() + extract.SetInputConnection(threshold.GetOutputPort()) + extract.AddCellType(vtk.VTK_QUAD) + extract.AddCellType(vtk.VTK_TRIANGLE) + extract.AddCellType(vtk.VTK_POLYGON) + extract.Update() + + if extract.GetOutputDataObject(0).GetNumberOfCells() != 0: + p = vtk.vtkPartitionedDataSet() + p.SetNumberOfPartitions(1) + p.SetPartition(0, extract.GetOutputDataObject(0)) + collection.SetPartitionedDataSet(count, p) + + collection.GetMetaData(count).Set( + vtk.vtkCompositeDataSet.NAME(), "Surface" + str(i - 1) + ) + + node = assembly.AddNode("Surface", id_surf) # + str(i - 1) + assembly.SetAttribute(node, "label", "Surface" + str(i - 1)) + # assembly.SetAttribute(id_surf_i, "type", TreeViewNodeType.REPRESENTATION) + # assembly.SetAttribute(id_surf_i, "number_of_partitions", collection.GetNumberOfPartitions(count)); + assembly.AddDataSetIndex(node, count) + count = count + 1 + + # load regions + for i in range(int(attr_min), int(attr_max + 1)): + threshold = vtk.vtkThreshold() + threshold.SetInputData(ugrid) + threshold.SetUpperThreshold(i) + threshold.SetLowerThreshold(i) + threshold.SetInputArrayToProcess( + 0, 0, 0, vtk.vtkDataObject.FIELD_ASSOCIATION_CELLS, attr + ) + + extract = vtk.vtkExtractCellsByType() + extract.SetInputConnection(threshold.GetOutputPort()) + extract.AddCellType(vtk.VTK_HEXAHEDRON) + extract.AddCellType(vtk.VTK_TETRA) + extract.AddCellType(vtk.VTK_WEDGE) + extract.AddCellType(vtk.VTK_PYRAMID) + extract.AddCellType(vtk.VTK_VOXEL) + extract.AddCellType(vtk.VTK_PENTAGONAL_PRISM) + extract.AddCellType(vtk.VTK_HEXAGONAL_PRISM) + extract.AddCellType(vtk.VTK_POLYHEDRON) + extract.Update() + + if extract.GetOutputDataObject(0).GetNumberOfCells() != 0: + p = vtk.vtkPartitionedDataSet() + p.SetNumberOfPartitions(1) + p.SetPartition(0, extract.GetOutputDataObject(0)) + collection.SetPartitionedDataSet(count, p) + + collection.GetMetaData(count).Set( + vtk.vtkCompositeDataSet.NAME(), "Region" + str(i - 1) + ) + + node = assembly.AddNode("Region", id_mesh) # + str(i - 1) + assembly.SetAttribute(node, "label", "Region" + str(i - 1)) + # assembly.SetAttribute(node, "type", TreeViewNodeType.REPRESENTATION) + # assembly.SetAttribute(node, "number_of_partitions", collection.GetNumberOfPartitions(count)); + assembly.AddDataSetIndex(node, count) + count = count + 1 + + elif path.suffix in COMPOSITE_DATA_READERS: + try: + Reader = COMPOSITE_DATA_READERS[path.suffix] + except KeyError as err: + # raise ValueError( + # f"`read` does not support a file with the {path.suffix} extension" + # ) from err + return 0 + + reader = Reader() + reader.SetFileName(path) + reader.Update() + + mb = reader.GetOutput() + + mainBlockName = "main" + faceBlocks = [] + if "mainBlockName" in mesh.attrib: + mainBlockName = mesh.attrib["mainBlockName"] + + # if "faceBlocks" in mesh.attrib: + # names = mesh.attrib["faceBlocks"] + # names = names.replace("{", "[").replace("}", "]") + # e = names.strip("][").split(",") + # e = [element.strip() for element in e] + # faceBlocks = e + + for i in range(mb.GetNumberOfBlocks()): + if mb.HasMetaData(i): + unstructuredGrid = vtk.vtkUnstructuredGrid.SafeDownCast(mb.GetBlock(i)) + if unstructuredGrid and unstructuredGrid.GetNumberOfPoints(): + blockName = mb.GetMetaData(i).Get(vtk.vtkCompositeDataSet.NAME()) + + p = vtk.vtkPartitionedDataSet() + p.SetNumberOfPartitions(1) + p.SetPartition(0, unstructuredGrid) + collection.SetPartitionedDataSet(count, p) + + collection.GetMetaData(count).Set( + vtk.vtkCompositeDataSet.NAME(), blockName + ) + + node = None + if blockName == mainBlockName: + node = assembly.AddNode("Region", id_mesh) # + else: + node = assembly.AddNode("Surface", id_surf) # + str(i - 1) + + + assembly.SetAttribute(node, "label", blockName) + # assembly.SetAttribute(id_surf_i, "type", TreeViewNodeType.REPRESENTATION) + # assembly.SetAttribute(id_surf_i, "number_of_partitions", collection.GetNumberOfPartitions(count)); + assembly.AddDataSetIndex(node, count) + count = count + 1 + + + + + return 1 + +def _read_vtkmesh( + file_path: str, + mesh: ElementTree.Element, + collection: vtk.vtkPartitionedDataSetCollection, + attr: str, +) -> int: + """Reads the mesh added in the simulation deck and builds adds it as a partition + + Args: + file_path (str): Path where the mesh is + mesh (ElementTree.Element): XML node of the mesh + collection (vtk.vtkPartitionedDataSetCollection): current DataAssembly + + Returns: + vtk.vtkPartitionedDataSet: The vtk mesh as a partition + """ + assembly = collection.GetDataAssembly() + + path = Path(file_path) + reader = pv.get_reader(path / mesh.attrib["file"]) + + idNode = assembly.AddNode("Mesh") + + assembly.SetAttribute(idNode, "label", mesh.attrib["name"]) + assembly.SetAttribute(idNode, "type", TreeViewNodeType.REPRESENTATION) + + # add vtu file as a partition of a partionedDataSet + p = vtk.vtkPartitionedDataSet() + p.SetPartition(0, reader.read()) + assembly.AddDataSetIndex(idNode, 0) + + # add partitionedDataSet to collection + collection.SetPartitionedDataSet(0, p) + + return 1 + +def _generate_grid( + mesh: ElementTree.Element, collection: vtk.vtkPartitionedDataSetCollection +) -> int: + """Generates the grid depending on the parameters read from the deck + + Args: + mesh (ElementTree.Element): XML node of the mesh + assembly (vtk.vtkDataAssembly): current DataAssembly + + Returns: + vtk.vtkPartitionedDataSet: The collection updated with the grid + """ + count: int = collection.GetNumberOfPartitionedDataSets() + + elem_type = mesh.attrib["elementTypes"].strip("}{ ") + + if elem_type == "C3D8": + xcoords = mesh.attrib["xCoords"] + ycoords = mesh.attrib["yCoords"] + zcoords = mesh.attrib["zCoords"] + xcoords_array = np.array(literal_eval(xcoords.translate(tr)), dtype=np.float64) + ycoords_array = np.array(literal_eval(ycoords.translate(tr)), dtype=np.float64) + zcoords_array = np.array(literal_eval(zcoords.translate(tr)), dtype=np.float64) + nx = literal_eval(mesh.attrib["nx"].translate(tr)) + ny = literal_eval(mesh.attrib["ny"].translate(tr)) + nz = literal_eval(mesh.attrib["nz"].translate(tr)) + + grid = vtk.vtkImageData() + + grid.dimensions = np.array((nx[0] + 1, ny[0] + 1, nz[0] + 1), dtype=np.int64) + + xspacing = (xcoords_array[1] - xcoords_array[0]) / grid.dimensions[0] + yspacing = (ycoords_array[1] - ycoords_array[0]) / grid.dimensions[1] + zspacing = (zcoords_array[1] - zcoords_array[0]) / grid.dimensions[2] + + # # Edit the spatial reference + grid.origin = ( + xcoords_array[0], + ycoords_array[0], + zcoords_array[0], + ) # The bottom left corner of the data set + grid.spacing = ( + xspacing, + yspacing, + zspacing, + ) # These are the cell sizes along each axis + + # idNode = assembly.AddNode("Mesh") + + # assembly.SetAttribute(idNode, "label", mesh.attrib["name"]) + # assembly.SetAttribute(idNode, "type", TreeViewNodeType.REPRESENTATION) + + # add vtu file as a partition of a partionedDataSet + p = vtk.vtkPartitionedDataSet() + p.SetPartition(0, grid) + collection.SetPartitionedDataSet(count, p) + count = count + 1 + # assembly.AddDataSetIndex(idNode, 0) + + return 1 + + else: + raise Exception("\nElem type {elem_type} of InternalMesh not handle yet") + + + +def _merge_xml_nodes( + existingNode: ElementTree.Element, targetNode: ElementTree.Element, level: int +) -> None: + """Merge nodes in an included file into the current structure level by level. + + Args: + existingNode (lxml.etree.Element): The current node in the base xml structure. + targetNode (lxml.etree.Element): The node to insert. + level (int): The xml file depth. + """ + # Copy attributes on the current level + for tk in targetNode.attrib.keys(): + existingNode.set(tk, targetNode.get(tk)) + + # Copy target children into the xml structure + currentTag = "" + matchingSubNodes = [] + + for target in targetNode.getchildren(): + insertCurrentLevel = True + + # Check to see if a node with the appropriate type + # exists at this level + if currentTag != target.tag: + currentTag = target.tag + matchingSubNodes = existingNode.findall(target.tag) + + if matchingSubNodes: + targetName = target.get("name") + + # Special case for the root Problem node (which may be unnamed) + if level == 0: + insertCurrentLevel = False + _merge_xml_nodes(matchingSubNodes[0], target, level + 1) + + # Handle named xml nodes + elif targetName and (currentTag not in ["Nodeset"]): + for match in matchingSubNodes: + if match.get("name") == targetName: + insertCurrentLevel = False + _merge_xml_nodes(match, target, level + 1) + + # Insert any unnamed nodes or named nodes that aren't present + # in the current xml structure + if insertCurrentLevel: + existingNode.insert(-1, target) + + +def _merge_included_xml_files( + root: ElementTree.Element, + file_path: str, + fname: str, + includeCount: int, + maxInclude: int = 100, +) -> None: + """Recursively merge included files into the current structure. + + Args: + root (lxml.etree.Element): The root node of the base xml structure. + fname (str): The name of the target xml file to merge. + includeCount (int): The current recursion depth. + maxInclude (int): The maximum number of xml files to include (default = 100) + """ + included_file_path = Path(expandvars(file_path), fname) + expanded_file = included_file_path.expanduser().resolve() + + # Check to see if the code has fallen into a loop + includeCount += 1 + if includeCount > maxInclude: + raise Exception( + "Reached maximum recursive includes... Is there an include loop?" + ) + + # Check to make sure the file exists + if not included_file_path.is_file(): + print("Included file does not exist: %s" % (included_file_path)) + raise Exception("Check included file path!") + + # Load target xml + try: + parser = ElementTree.XMLParser(remove_comments=True, remove_blank_text=True) + includeTree = ElementTree.parse(included_file_path, parser) + includeRoot = includeTree.getroot() + except XMLSyntaxError as err: + print("\nCould not load included file: %s" % (included_file_path)) + print(err.msg) + raise Exception("\nCheck included file!") from err + + # Recursively add the includes: + for include_node in includeRoot.findall("Included"): + for f in include_node.findall("File"): + _merge_included_xml_files( + root, expanded_file.parent, f.get("name"), includeCount + ) + + # Merge the results into the xml tree + _merge_xml_nodes(root, includeRoot, 0) + + +def format_attribute(attribute_indent: str, ka: str, attribute_value: str) -> str: + """Format xml attribute strings + + Args: + attribute_indent (str): Attribute indent string + ka (str): Attribute name + attribute_value (str): Attribute value + + Returns: + str: Formatted attribute value + """ + # Make sure that a space follows commas + attribute_value = re.sub(r",\s*", ", ", attribute_value) + + # Handle external brackets + attribute_value = re.sub(r"{\s*", "{ ", attribute_value) + attribute_value = re.sub(r"\s*}", " }", attribute_value) + + # Consolidate whitespace + attribute_value = re.sub(r"\s+", " ", attribute_value) + + # Identify and split multi-line attributes + if re.match(r"\s*{\s*({[-+.,0-9a-zA-Z\s]*},?\s*)*\s*}", attribute_value): + split_positions: List[Any] = [ + match.end() for match in re.finditer(r"}\s*,", attribute_value) + ] + newline_indent = "\n%s" % (" " * (len(attribute_indent) + len(ka) + 4)) + new_values = [] + for a, b in zip([None] + split_positions, split_positions + [None]): + new_values.append(attribute_value[a:b].strip()) + if new_values: + attribute_value = newline_indent.join(new_values) + + return attribute_value + + +def format_xml_level( + output: TextIO, + node: ElementTree.Element, + level: int, + indent: str = " " * 2, + block_separation_max_depth: int = 2, + modify_attribute_indent: bool = False, + sort_attributes: bool = False, + close_tag_newline: bool = False, + include_namespace: bool = False, +) -> None: + """Iteratively format the xml file + + Args: + output (file): the output text file handle + node (lxml.etree.Element): the current xml element + level (int): the xml depth + indent (str): the xml indent style + block_separation_max_depth (int): the maximum depth to separate adjacent elements + modify_attribute_indent (bool): option to have flexible attribute indentation + sort_attributes (bool): option to sort attributes alphabetically + close_tag_newline (bool): option to place close tag on a separate line + include_namespace (bool): option to include the xml namespace in the output + """ + + # Handle comments + if node.tag is ElementTree.Comment: + output.write("\n%s" % (indent * level, node.text)) + + else: + # Write opening line + opening_line = "\n%s<%s" % (indent * level, node.tag) + output.write(opening_line) + + # Write attributes + if len(node.attrib) > 0: + # Choose indentation + attribute_indent = "%s" % (indent * (level + 1)) + if modify_attribute_indent: + attribute_indent = " " * (len(opening_line)) + + # Get a copy of the attributes + attribute_dict = {} + if (level == 0) & include_namespace: + # Handle the optional namespace information at the root level + # Note: preferably, this would point to a schema we host online + attribute_dict[ + "xmlns:xsi" + ] = "http://www.w3.org/2001/XMLSchema-instance" + attribute_dict[ + "xsi:noNamespaceSchemaLocation" + ] = "/usr/gapps/GEOS/schema/schema.xsd" + elif level > 0: + attribute_dict = node.attrib + + # Sort attribute names + akeys = list(attribute_dict.keys()) + if sort_attributes: + akeys = sorted(akeys) + + # Format attributes + for ka in akeys: + # Avoid formatting mathpresso expressions + if not ( + node.tag in ["SymbolicFunction", "CompositeFunction"] + and ka == "expression" + ): + attribute_dict[ka] = format_attribute( + attribute_indent, ka, attribute_dict[ka] + ) + + for ii in range(0, len(akeys)): + k = akeys[ii] + if (ii == 0) & modify_attribute_indent: + output.write(' %s="%s"' % (k, attribute_dict[k])) + else: + output.write( + '\n%s%s="%s"' % (attribute_indent, k, attribute_dict[k]) + ) + + # Write children + if len(node): + output.write(">") + Nc = len(node) + for ii, child in zip(range(Nc), node): + format_xml_level( + output, + child, + level + 1, + indent, + block_separation_max_depth, + modify_attribute_indent, + sort_attributes, + close_tag_newline, + include_namespace, + ) + + # Add space between blocks + if ( + (level < block_separation_max_depth) + & (ii < Nc - 1) + & (child.tag is not ElementTree.Comment) + ): + output.write("\n") + + # Write the end tag + output.write("\n%s" % (indent * level, node.tag)) + else: + if close_tag_newline: + output.write("\n%s/>" % (indent * level)) + else: + output.write("/>") + + +def format_xml( + tree: ElementTree.ElementTree, + indent_size: int = 2, + indent_style: bool = False, + block_separation_max_depth: int = 2, + alphebitize_attributes: bool = False, + close_style: bool = False, + namespace: bool = False, +) -> io.StringIO: + # tree = ElementTree.parse(fname) + root = tree.getroot() + prologue_comments = [tmp.text for tmp in root.itersiblings(preceding=True)] + epilog_comments = [tmp.text for tmp in root.itersiblings()] + + # with open(fname, "w") as f: + f = io.StringIO() + f.write('\n') + + for comment in reversed(prologue_comments): + f.write("\n" % (comment)) + + format_xml_level( + f, + root, + 0, + indent=" " * indent_size, + block_separation_max_depth=block_separation_max_depth, + modify_attribute_indent=indent_style, + sort_attributes=alphebitize_attributes, + close_tag_newline=close_style, + include_namespace=namespace, + ) + + for comment in epilog_comments: + f.write("\n" % (comment)) + f.write("\n") + + return f + + +def format_deck( + input_fname: str, + indent_size: int = 2, + indent_style: bool = False, + block_separation_max_depth: int = 2, + alphebitize_attributes: bool = False, + close_style: bool = False, + namespace: bool = False, +) -> None: + """Script to format xml files + + Args: + input_fname (str): Input file name + indent_size (int): Indent size + indent_style (bool): Style of indentation (0=fixed, 1=hanging) + block_separation_max_depth (int): Max depth to separate xml blocks + alphebitize_attributes (bool): Alphebitize attributes + close_style (bool): Style of close tag (0=same line, 1=new line) + namespace (bool): Insert this namespace in the xml description + """ + fname = os.path.expanduser(input_fname) + try: + tree = ElementTree.parse(fname) + root = tree.getroot() + prologue_comments = [tmp.text for tmp in root.itersiblings(preceding=True)] + epilog_comments = [tmp.text for tmp in root.itersiblings()] + + with open(fname, "w") as f: + f.write('\n') + + for comment in reversed(prologue_comments): + f.write("\n" % (comment)) + + format_xml_level( + f, + root, + 0, + indent=" " * indent_size, + block_separation_max_depth=block_separation_max_depth, + modify_attribute_indent=indent_style, + sort_attributes=alphebitize_attributes, + close_tag_newline=close_style, + include_namespace=namespace, + ) + + for comment in epilog_comments: + f.write("\n" % (comment)) + f.write("\n") + + except ElementTree.ParseError as err: + print("\nCould not load file: %s" % (fname)) + print(err.msg) + raise Exception("\nCheck input file!") diff --git a/geos-xml-viewer/src/geos_xml_viewer/algorithms/write_wells.py b/geos-xml-viewer/src/geos_xml_viewer/algorithms/write_wells.py new file mode 100644 index 00000000..f27786a0 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/algorithms/write_wells.py @@ -0,0 +1,317 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import numpy +import vtk + + +class CellLocator: + def __init__(self, fileName): + self.globalGrid = None + self.locator = None + self.pointLocator = None + self._read_grid(fileName) + self._create_locator() + + localPoints = vtk.vtkPoints() + self.merge = vtk.vtkMergePoints() + self.localGrid = vtk.vtkUnstructuredGrid() + bounds = self.globalGrid.GetBounds() + self.z = bounds[4:6] + self.t = vtk.reference(-1.0e30) + self.pcoords = [-1.0] * 3 + self.subId = vtk.reference(-1) + self.merge.InitPointInsertion(localPoints, bounds) + self.localGrid.SetPoints(localPoints) + + def locate(self, x): + foundIndex, xr = None, x + cellids = vtk.vtkIdList() + x1, x2 = (x[0], x[1], self.z[0]), (x[0], x[1], self.z[1]) + self.locator.FindCellsAlongLine(x1, x2, 1.0e-4, cellids) + cellCount = cellids.GetNumberOfIds() + gridPoints = self.globalGrid.GetPoints() + for ci in range(cellCount): + cellIndex = cellids.GetId(ci) + cell = self.globalGrid.GetCell(cellIndex) + + intersections = [] + for faceIndex in range(cell.GetNumberOfFaces()): + face = cell.GetFace(faceIndex) + facePointCount = face.GetNumberOfPoints() + faceCentre = numpy.mean( + numpy.array( + [ + gridPoints.GetPoint(face.GetPointId(fi)) + for fi in range(facePointCount) + ] + ), + axis=0, + ) + for i in range(facePointCount): + xc0 = gridPoints.GetPoint(face.GetPointId((i + 0) % facePointCount)) + xc1 = gridPoints.GetPoint(face.GetPointId((i + 1) % facePointCount)) + xc2 = faceCentre + trianglePoints = [-1] * 3 + for ip, xp in enumerate([xc0, xc1, xc2]): + self.merge.InsertUniquePoint(xp, self.subId) + trianglePoints[ip] = self.subId.get() + newCell = self.localGrid.InsertNextCell( + vtk.VTK_TRIANGLE, 3, trianglePoints + ) + triangle = self.localGrid.GetCell(newCell) + xp = [-1.0e30] * 3 + res = triangle.IntersectWithLine( + x1, x2, 1.0e-4, self.t, xp, self.pcoords, self.subId + ) + if res != 0: + intersections.append(xp[2]) + + zz = sorted({int(i / 1.0e-3): i for i in intersections}.values()) + if len(zz) == 2: + if (zz[0] <= x[2]) and (x[2] <= zz[1]): + foundIndex = cellIndex + xr = (x[0], x[1], 0.5 * (zz[0] + zz[1])) + break + + return foundIndex, xr + + def _read_grid(self, fileName): + print("Reading mesh %s" % (fileName), flush=True, end=" ... ") + reader = vtk.vtkXMLUnstructuredGridReader() + reader.SetFileName(fileName) + reader.Update() + print("[Done]", flush=True) + self.globalGrid = reader.GetOutput() + + def _create_locator(self): + print("Building cell locator", flush=True, end=" ... ") + cellLocator = vtk.vtkCellLocator() + cellLocator.SetDataSet(self.globalGrid) + cellLocator.BuildLocator() + print("[Done]", flush=True) + self.locator = cellLocator + + +def translate_connections(connections): + dx, dy = 2493.0, 531520.0 + for name in connections: + x, y, z = connections[name]["x"] + connections[name]["x"] = (x + dx, y + dy, -z) + + +def locate_connections(connections, cellLocator): + print("Locating connections", flush=True) + connectionCount = len(connections) + for _, connection in connections.items(): + index, xg = cellLocator.locate(connection["x"]) + assert index is not None + connection["v"] = (index, xg) + + +def filter_connections(connections, grid): + fiteredConnections = {} + attributeArray = grid.GetCellData().GetArray("attribute", vtk.reference(-1)) + assert attributeArray is not None + selectedRegions = set([3]) + print("Filtering connections", flush=True) + connectionCount = len(connections) + for name, connection in connections.items(): + cellIndex = connection["v"][0] + cellAttribute = attributeArray.GetValue(cellIndex) + if cellAttribute in selectedRegions: + fiteredConnections[name] = connection + return fiteredConnections + + +def sort_connections(connections, grid): + wells = {} + TF = 0.001 * 1.157407407407407e-05 * 1.0e-05 + print("Sorting connections", flush=True) + connectionCount = len(connections) + for _, connection in connections.items(): + wellName = connection["w"] + cellIndex = connection["v"][0] + cell = grid.GetCell(cellIndex) + bounds = cell.GetBounds() + + if wellName not in wells: + wells[wellName] = [] + wells[wellName].append( + { + "x": connection["x"], + "g": connection["g"], + "l": connection["l"][0], + "v": cellIndex, + "t": TF * connection["t"], + "b": bounds, + } + ) + for wellName in wells: + wells[wellName] = sorted(wells[wellName], key=lambda c: -c["x"][2]) + + return wells + + +def write_fluxes(wells, fileName, cellLocator): + strGeometry, strFlux, strFunction = "", "", "" + xtol, ztol = 1.0, 1.0e-2 + print("Writing wells", flush=True) + wellCount = len(wells) + for wellName, wellData in wells.items(): + bb = wellData[0]["b"] + xx, yy, zz = numpy.array([bb[0], bb[1]]), numpy.array([bb[2], bb[3]]), [] + for c in wellData: + bb = c["b"] + xx = numpy.array([min(xx[0], bb[0]), max(xx[1], bb[1])]) + yy = numpy.array([min(yy[0], bb[2]), max(yy[1], bb[3])]) + z0, z1 = bb[4], bb[5] + found = False + for zi, dz in enumerate(zz): + if (dz[0] < z0 + ztol and z0 - ztol < dz[1]) or ( + dz[0] < z1 + ztol and z1 - ztol < dz[1] + ): + found = True + zz[zi] = [min(dz[0], z0), max(dz[1], z1)] + break + if not found: + zz.append([z0, z1]) + + boxNames = [] + boxCount = len(zz) + for zi, dz in enumerate(zz): + boxName = "%s.%03d" % (wellName, zi + 1) + boxNames.append(boxName) + xMin = "{ %.5e, %.5e, %.5e }" % (xx[0] - xtol, yy[0] - xtol, dz[0] - ztol) + xMax = "{ %.5e, %.5e, %.5e }" % (xx[1] + xtol, yy[1] + xtol, dz[1] + ztol) + + strGeometry += """{tab} +""".format(tab=" ", name=boxName, xMin=xMin, xMax=xMax) + + strFlux += """{tab} +""".format(tab=" ", name=f"FLUX.{wellName}", setNames=", ".join(boxNames)) + + strFunction += """{tab} +""".format(tab=" ", name=f"FLUX.{wellName}") + + with open(fileName, mode="w", encoding="utf-8") as xml: + xml.write('\n\n') + xml.write(f" \n{strGeometry} \n") + xml.write(f" \n{strFlux} \n") + xml.write(f" \n{strFunction} \n") + xml.write("\n\n") + + +def write_solver(wells, fileName): + strControls, strMesh, strFunction = "", "", "" + tab = " " + ztol = 1.0e-3 + targetRegions = [] + for wellName, wellData in wells.items(): + Z = [zz for w in wellData for zz in w["b"][4:]] + cz = [w["x"][2] for w in wellData] + nc = len(cz) + Z.extend([0.5 * (cz[i - 1] + cz[i]) for i in range(1, nc)]) + Z = {int(z / ztol): z for z in Z}.values() + Z = sorted(Z, reverse=True) + nz = len(Z) + x, y = wellData[0]["x"][:2] # Assume vertical wells + z0 = Z[0] + coords, conns, perforations = "", "", "" + + coords = f",\n{tab} ".join( + ["{ %.4e, %.4e, %.4e }" % (x, y, z) for z in Z] + ) + conns = ",".join(["{%d,%d}" % (i - 1, i) for i in range(1, nz)]) + + targetRegions.append(f"WELL.{wellName}") + + for c in wellData: + lgrName = "" if c["l"] is None else f"{c['l']}." + boxName = "%s.%s%03d.%03d.%03d" % ( + wellName, + lgrName, + c["g"][0], + c["g"][1], + c["g"][2], + ) + distance = z0 - c["x"][2] + trans = c["t"] + + newNode = ElementTree.Element("Perforation") + + target = root.find(".//holidays") + target.append(newNode) + + from geos.models.schema import PerforationType + + pt = PerforationType(boxName, distance, trans) + print(pt) + + perforations += f"""\n{tab} """ + + strMesh += f"""{tab}{perforations} +{tab} +""" + + strFunction += """{tab} +""".format(tab=" ", name=f"FLUX.{wellName}") + + strControls += """{tab} +""".format(tab=" ", name=wellName, z0=z0) + + with open(fileName, mode="w", encoding="utf-8") as xml: + xml.write('\n\n') + xml.write(" \n") + xml.write( + """ +""".format(targetRegions=", ".join(targetRegions)) + ) + xml.write(strControls) + xml.write(" \n") + xml.write(" \n") + xml.write( + f" \n \n{strMesh} \n \n" + ) + xml.write(f" \n{strFunction} \n") + xml.write("\n\n") diff --git a/geos-xml-viewer/src/geos_xml_viewer/bin/exporter.py b/geos-xml-viewer/src/geos_xml_viewer/bin/exporter.py new file mode 100644 index 00000000..21fb3149 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/bin/exporter.py @@ -0,0 +1,92 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import argparse +from pathlib import PurePath + +from geos_xml_viewer.filters.geosDeckReader import GeosDeckReader +from vtkmodules.vtkIOParallelXML import ( + vtkXMLPartitionedDataSetCollectionWriter, +) + + +def valid_file(param: str) -> str: + """File validation function for argparse for .vtpc files. + + Args: + param (str): filepath to a .vtpc + + Raises: + argparse.ArgumentTypeError: Raises an error if the file does not have a .vtpc extension + + Returns: + str: filepath to a.vtpc + """ + ext: str = PurePath(param).suffix + if ext.lower() != ".vtpc": + raise argparse.ArgumentTypeError("File must have a .vtpc extension") + return param + + +def parsing() -> argparse.ArgumentParser: + """Argument parsing function. + + Returns: + argparse.ArgumentParser: argument list + """ + parser = argparse.ArgumentParser( + description="Extract Internal wells into VTK files" + ) + + parser.add_argument( + "-xp", + "--xmlFilepath", + type=str, + default="", + help="path to xml file.", + required=True, + ) + parser.add_argument( + "-a", + "--attributeName", + type=str, + default="attribute", + help="Attribute name.", + required=False, + ) + parser.add_argument( + "-o", + "--outputName", + type=valid_file, + default="myPartionedDataSetCollection.vtpc", + help="name of the output file.", + ) + + return parser + + +def main(args: argparse.Namespace) -> None: + """Main function that reads the xml file and writes a PartiotionedDataSetCollection file. + + Args: + args (argparse.Namespace): list of arguments + """ + reader = GeosDeckReader() + reader.SetFileName(args.xmlFilepath) + reader.SetAttributeName(args.attributeName) + writer = vtkXMLPartitionedDataSetCollectionWriter() + writer.SetInputConnection(reader.GetOutputPort()) + writer.SetFileName(args.outputName) + writer.Write() + + +def run() -> None: + """Parses the arguments and runs the main function.""" + parser = parsing() + args, unknown_args = parser.parse_known_args() + main(args) + + +if __name__ == "__main__": + run() diff --git a/geos-xml-viewer/src/geos_xml_viewer/bin/modifier.py b/geos-xml-viewer/src/geos_xml_viewer/bin/modifier.py new file mode 100644 index 00000000..47ff6d5f --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/bin/modifier.py @@ -0,0 +1,105 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import argparse +from pathlib import PurePath + +import vtkmodules.all as vtk +from geos_xml_viewer.filters.geosDeckReader import GeosDeckReader + + +def valid_file(param: str) -> str: + ext: str = PurePath(param).suffix + if ext.lower() != ".vtpc": + raise argparse.ArgumentTypeError("File must have a .vtpc extension") + return param + + +def parsing() -> argparse.ArgumentParser: + parser = argparse.ArgumentParser(description="Rewrite wells into VTK file") + + parser.add_argument( + "-xp", + "--xmlFilepath", + type=str, + default="", + help="path to xml file.", + required=True, + ) + parser.add_argument( + "-a", + "--attributeName", + type=str, + default="attribute", + help="Attribute name.", + required=False, + ) + parser.add_argument( + "-vtpc", + type=str, + default="", + help="path to vtpc file.", + required=True, + ) + parser.add_argument( + "-o", + "--outputName", + type=valid_file, + default="myModifiedPartionedDataSetCollection.vtpc", + help="name of the output file.", + ) + + return parser + + +def main(args: argparse.Namespace) -> None: + reader = GeosDeckReader() + reader.SetFileName(args.xmlFilepath) + reader.SetAttributeName(args.attributeName) + reader.Update() + pdsc_xml = reader.GetOutputDataObject(0) + + vtpc = vtk.vtkXMLPartitionedDataSetCollectionReader() + vtpc.SetFileName(args.vtpc) + vtpc.Update() + pdsc_file = vtpc.GetOutput() + + # look for xml root node name and wells node id + assembly_xml: vtk.vtkDataAssembly = pdsc_xml.GetDataAssembly() + root_name_xml: str = assembly_xml.GetNodeName(assembly_xml.GetRootNode()) + wells_xml = assembly_xml.GetFirstNodeByPath("//" + root_name_xml + "/Wells") + + # look for vtpc root node name and wells node id + assembly_file: vtk.vtkDataAssembly = pdsc_file.GetDataAssembly() + wells_file = assembly_file.GetFirstNodeByPath("//" + root_name_xml + "/Wells") + + print("assembly from vtpc file: ", wells_file) + print("wells id from vtpc file: ", wells_file) + print("remove dataset indices....") + # remove all well's subnode from file + assembly_file.RemoveAllDataSetIndices(wells_file) + print("... finished") + print("remove nodes...") + assembly_file.RemoveNode(wells_file) + print("... finished") + print(assembly_file) + print(wells_xml) + assembly_file.AddSubtree(assembly_file.GetRootNode(), assembly_xml, wells_xml) + + print(assembly_file) + + writer = vtk.vtkXMLPartitionedDataSetCollectionWriter() + writer.SetInputData(pdsc_file) + writer.SetFileName(args.outputName) + writer.Write() + + +def run() -> None: + parser = parsing() + args, unknown_args = parser.parse_known_args() + main(args) + + +if __name__ == "__main__": + run() diff --git a/geos-xml-viewer/src/geos_xml_viewer/bin/splitter.py b/geos-xml-viewer/src/geos_xml_viewer/bin/splitter.py new file mode 100644 index 00000000..523135bc --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/bin/splitter.py @@ -0,0 +1,115 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import argparse +from pathlib import PurePath + +from geos_xml_viewer.algorithms.deck import SimulationDeck, read, format_xml +from lxml import etree as ElementTree # type: ignore[import-untyped] + + +def valid_file(param: str) -> str: + """File validation function for argparse for .vtpc files. + + Args: + param (str): filepath to a .vtpc + + Raises: + argparse.ArgumentTypeError: Raises an error if the file does not have a .vtpc extension + + Returns: + str: filepath to a.vtpc + """ + ext: str = PurePath(param).suffix + if ext.lower() != ".vtpc": + raise argparse.ArgumentTypeError("File must have a .vtpc extension") + return param + + +def parsing() -> argparse.ArgumentParser: + """Argument parsing function. + + Returns: + argparse.ArgumentParser: argument list + """ + parser = argparse.ArgumentParser( + description="Extract Internal wells into VTK files" + ) + + parser.add_argument( + "-xp", + "--xmlFilepath", + type=str, + default="", + help="path to xml file.", + required=True, + ) + + parser.add_argument( + "--deckName", + type=str, + default="test", + help="name of the deck.", + required=True, + ) + + return parser + + +def split_by_components(simulation_deck: SimulationDeck, deck_name: str) -> None: + # Top-level elements + top_elements = simulation_deck.xml_root.findall("./") + + # create root document + output_root = ElementTree.Element("Problem") + + includes = ElementTree.SubElement(output_root, "Included") + for t in top_elements: + ElementTree.SubElement( + includes, "File", attrib={"name": deck_name + "_" + t.tag + ".xml"} + ) + + tree = ElementTree.ElementTree(output_root) + ElementTree.indent(tree) + + # create files for top elements + for f in top_elements: + subtree_root = ElementTree.Element("Problem") + subtree_root.append(f) + + subtree = ElementTree.ElementTree(subtree_root) + + ElementTree.indent(subtree) + filename = deck_name + "_" + f.tag + ".xml" + with open(filename, "wb") as files: + # format_xml(subtree) + subtree.write( + files, encoding="UTF-8", xml_declaration=True, pretty_print=True + ) + + filename = deck_name + ".xml" + with open(filename, "wb") as files: + # tree = format_xml(tree) + tree.write(files, encoding="UTF-8", xml_declaration=True, pretty_print=True) + + +def main(args: argparse.Namespace) -> None: + """Main function that reads the xml file and writes a PartiotionedDataSetCollection file. + + Args: + args (argparse.Namespace): list of arguments + """ + simulation_deck: SimulationDeck = read(args.xmlFilepath) + split_by_components(simulation_deck, args.deckName) + + +def run() -> None: + """Parses the arguments and runs the main function.""" + parser = parsing() + args, unknown_args = parser.parse_known_args() + main(args) + + +if __name__ == "__main__": + run() diff --git a/geos-xml-viewer/src/geos_xml_viewer/bin/testCellLocator.py b/geos-xml-viewer/src/geos_xml_viewer/bin/testCellLocator.py new file mode 100644 index 00000000..e4ebbc68 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/bin/testCellLocator.py @@ -0,0 +1,330 @@ +import argparse + +import pyvista as pv +from vtkmodules.vtkCommonCore import ( + reference, + vtkIdList, +) +from vtkmodules.vtkCommonDataModel import ( + vtkCellLocator, + vtkCellTreeLocator, + vtkDataAssembly, + vtkGenericCell, + vtkPartitionedDataSetCollection, + vtkStaticCellLocator, +) +from vtkmodules.vtkCommonSystem import vtkTimerLog +from vtkmodules.vtkFiltersCore import ( + vtkAppendFilter, +) +from vtkmodules.vtkFiltersFlowPaths import vtkModifiedBSPTree +from vtkmodules.vtkFiltersGeneral import ( + vtkOBBTree, +) +from vtkmodules.vtkIOXML import ( + vtkXMLPartitionedDataSetCollectionReader, +) + + +def parsing() -> argparse.ArgumentParser: + parser = argparse.ArgumentParser(description="Test Cell Locator onto VTK files") + + parser.add_argument( + "-vtpc", + "--vtpcFilepath", + type=str, + default="", + help="path to .vtpc file.", + required=True, + ) + + return parser + + +def main(args: argparse.Namespace) -> None: + reader = vtkXMLPartitionedDataSetCollectionReader() + reader.SetFileName(args.vtpcFilepath) + reader.Update() + pdsc: vtkPartitionedDataSetCollection = reader.GetOutput() + + assembly: vtkDataAssembly = pdsc.GetDataAssembly() + root_name: str = assembly.GetNodeName(assembly.GetRootNode()) + + # 1. Get Mesh + mesh = assembly.GetFirstNodeByPath("//" + root_name + "/Mesh") + + append_filter = vtkAppendFilter() + append_filter.SetMergePoints(True) + append_filter.SetTolerance(0.0) + if mesh > 0: + for sub_node in assembly.GetChildNodes(mesh, False): + datasets = assembly.GetDataSetIndices(sub_node, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + append_filter.AddInputData(dataset.GetPartition(0)) + else: + raise Exception("No mesh found") + + append_filter.Update() + output = append_filter.GetOutputDataObject(0) + + # 2. Get Perforations + # Create points array which are positions to probe data with + # FindCell(), We also create an array to hold the results of this + # probe operation. + # ProbeCells = vtkPoints() + # ProbeCells.SetDataTypeToDouble() + ProbeCells: list[pv.PointSet] = [] + wells = assembly.GetFirstNodeByPath("//" + root_name + "/Wells") + if wells > 0: + for well in assembly.GetChildNodes(wells, False): + sub_nodes = assembly.GetChildNodes(well, False) + for sub_node in sub_nodes: + if assembly.GetNodeName(sub_node) == "Perforations": + for i, perfos in enumerate(assembly.GetChildNodes(sub_node, False)): + datasets = assembly.GetDataSetIndices(perfos, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + if dataset.GetPartition(0) is not None: + pointset = dataset.GetPartition(0) + ProbeCells.append(pv.wrap(pointset)) + # ProbeCells.InsertNextPoint(pointset.GetPoint(0)) + else: + raise Exception("No wells found") + + # numProbes = ProbeCells.GetNumberOfPoints() + numProbes = len(ProbeCells) + + closest = vtkIdList() + closest.SetNumberOfIds(numProbes) + treeClosest = vtkIdList() + treeClosest.SetNumberOfIds(numProbes) + staticClosest = vtkIdList() + staticClosest.SetNumberOfIds(numProbes) + bspClosest = vtkIdList() + bspClosest.SetNumberOfIds(numProbes) + obbClosest = vtkIdList() + obbClosest.SetNumberOfIds(numProbes) + dsClosest = vtkIdList() + dsClosest.SetNumberOfIds(numProbes) + + genCell = vtkGenericCell() + pc = [0, 0, 0] + weights = [0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0] + subId = reference(0) + + # Print initial statistics + print(f"Processing NumCells: {output.GetNumberOfCells()}") + print("\n") + timer = vtkTimerLog() + + ############################################################# + # Time the creation and building of the static cell locator + locator2 = vtkStaticCellLocator() + locator2.SetDataSet(output) + locator2.AutomaticOn() + locator2.SetNumberOfCellsPerNode(20) + + timer.StartTimer() + locator2.BuildLocator() + timer.StopTimer() + time = timer.GetElapsedTime() + print(f"Build Static Cell Locator: {time}") + + # Probe the dataset with FindClosestPoint() and time it + timer.StartTimer() + for i, m in enumerate(ProbeCells): + staticClosest.SetId( + i, locator2.FindCell(m.GetPoint(0)) + ) # ,0.001,genCell,pc,weights)) + # for i in range (0,numProbes): + # staticClosest.SetId(i, locator2.FindCell(ProbeCells.GetPoint(i)) #,0.001,genCell,pc,weights)) + timer.StopTimer() + opTime = timer.GetElapsedTime() + print(f" Find cell probing: {opTime}") + + # Time the deletion of the locator. The incremental locator is quite slow due + # to fragmented memory. + timer.StartTimer() + del locator2 + timer.StopTimer() + time2 = timer.GetElapsedTime() + print(f" Delete Static Cell Locator: {time2}") + print(f" Static Cell Locator (Total): {time + opTime + time2}") + print("\n") + + ############################################################# + # Time the creation and building of the standard cell locator + locator = vtkCellLocator() + locator.SetDataSet(output) + locator.SetNumberOfCellsPerBucket(25) + locator.AutomaticOn() + + timer.StartTimer() + locator.BuildLocator() + timer.StopTimer() + time = timer.GetElapsedTime() + print(f"Build Cell Locator: {time}") + + # Probe the dataset with FindClosestPoint() and time it + timer.StartTimer() + for i, m in enumerate(ProbeCells): + closest.SetId(i, locator.FindCell(m.GetPoint(0))) # ,0.001,genCell,pc,weights)) + # for i in range (0,numProbes): + # closest.SetId(i, locator.FindCell(ProbeCells.GetPoint(i),0.001,genCell,pc,weights)) + timer.StopTimer() + opTime = timer.GetElapsedTime() + print(f" Find cell probing: {opTime}") + + # Time the deletion of the locator. The standard locator is quite slow due + # to fragmented memory. + timer.StartTimer() + del locator + timer.StopTimer() + time2 = timer.GetElapsedTime() + print(f" Delete Cell Locator: {time2}") + print(f" Cell Locator (Total): {time + opTime + time2}") + print("\n") + + ############################################################# + # Time the creation and building of the cell tree locator + locator1 = vtkCellTreeLocator() + locator1.SetDataSet(output) + locator1.AutomaticOn() + + timer.StartTimer() + locator1.BuildLocator() + timer.StopTimer() + time = timer.GetElapsedTime() + print(f"Build Cell Tree Locator: {time}") + + # Probe the dataset with FindClosestPoint() and time it + timer.StartTimer() + for i, m in enumerate(ProbeCells): + treeClosest.SetId( + i, locator1.FindCell(m.GetPoint(0)) + ) # ,0.001,genCell,pc,weights)) + # for i in range (0,numProbes): + # treeClosest.SetId(i, locator1.FindCell(ProbeCells.GetPoint(i),0.001,genCell,pc,weights)) + timer.StopTimer() + opTime = timer.GetElapsedTime() + print(f" Find cell probing: {opTime}") + + # Time the deletion of the locator. The incremental locator is quite slow due + # to fragmented memory. + timer.StartTimer() + del locator1 + timer.StopTimer() + time2 = timer.GetElapsedTime() + print(f" Delete Cell Tree Locator: {time2}") + print(f" Cell Tree Locator (Total): {time + opTime + time2}") + print("\n") + + ############################################################# + # Time the creation and building of the bsp tree + locator3 = vtkModifiedBSPTree() + locator3.SetDataSet(output) + locator3.AutomaticOn() + + timer.StartTimer() + locator3.BuildLocator() + timer.StopTimer() + time = timer.GetElapsedTime() + print(f"Build BSP Tree Locator: {time}") + + # Probe the dataset with FindClosestPoint() and time it + timer.StartTimer() + for i, m in enumerate(ProbeCells): + bspClosest.SetId( + i, locator3.FindCell(m.GetPoint(0)) + ) # ,0.001,genCell,pc,weights)) + # for i in range (0,numProbes): + # bspClosest.SetId(i, locator3.FindCell(ProbeCells.GetPoint(i),0.001,genCell,pc,weights)) + timer.StopTimer() + opTime = timer.GetElapsedTime() + print(f" Find cell probing: {opTime}") + + # Time the deletion of the locator. The incremental locator is quite slow due + # to fragmented memory. + timer.StartTimer() + del locator3 + timer.StopTimer() + time2 = timer.GetElapsedTime() + print(f" Delete BSP Tree Locator: {time2}") + print(f" BSP Tree Locator (Total): {time + opTime + time2}") + print("\n") + + ############################################################# + # Time the creation and building of the obb tree + locator4 = vtkOBBTree() + locator4.SetDataSet(output) + locator4.AutomaticOn() + + timer.StartTimer() + locator4.BuildLocator() + timer.StopTimer() + time = timer.GetElapsedTime() + print(f"Build OBB Locator: {time}") + + # Probe the dataset with FindClosestPoint() and time it + timer.StartTimer() + for i, m in enumerate(ProbeCells): + obbClosest.SetId( + i, locator4.FindCell(m.GetPoint(0)) + ) # ,0.001,genCell,pc,weights)) + # for i in range (0,numProbes): + # obbClosest.SetId(i, locator4.FindCell(ProbeCells.GetPoint(i))) #,0.001,genCell,pc,weights)) + timer.StopTimer() + opTime = timer.GetElapsedTime() + print(f" Find cell probing: {opTime}") + + # Time the deletion of the locator. The incremental locator is quite slow due + # to fragmented memory. + timer.StartTimer() + del locator4 + timer.StopTimer() + time2 = timer.GetElapsedTime() + print(f" Delete OBB Locator: {time2}") + print(f" OBB Locator (Total): {time + opTime + time2}") + print("\n") + + ############################################################# + # For comparison purposes compare to FindCell() + timer.StartTimer() + + # output.FindCell(ProbeCells.GetPoint(0),genCell,-1,0.001,subId,pc,weights) + timer.StopTimer() + time = timer.GetElapsedTime() + print(f"Point Locator: {time}") + + # Probe the dataset with FindClosestPoint() and time it + timer.StartTimer() + for i, m in enumerate(ProbeCells): + dsClosest.SetId( + i, output.FindCell(m.GetPoint(0), genCell, -1, 0.001, subId, pc, weights) + ) + # for i in range (0,numProbes): + # dsClosest.SetId(i, output.FindCell(ProbeCells.GetPoint(0),genCell,-1,0.001,subId,pc,weights)) + timer.StopTimer() + opTime = timer.GetElapsedTime() + print(f" Find cell probing: {opTime}") + + # Time the deletion of the locator. The incremental locator is quite slow due + # to fragmented memory. + timer.StartTimer() + del output + timer.StopTimer() + time2 = timer.GetElapsedTime() + print(f" Delete Point Locator: {time2}") + print(f" Point Locator (Total): {time + opTime + time2}") + print("\n") + + +def run() -> None: + parser = parsing() + args, unknown_args = parser.parse_known_args() + main(args) + + +if __name__ == "__main__": + run() diff --git a/geos-xml-viewer/src/geos_xml_viewer/bin/validate.py b/geos-xml-viewer/src/geos_xml_viewer/bin/validate.py new file mode 100644 index 00000000..3b844287 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/bin/validate.py @@ -0,0 +1,49 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import argparse + +from xmlschema import XMLSchema + + +def parsing() -> argparse.ArgumentParser: + parser = argparse.ArgumentParser(description="Validate xsd schema") + + parser.add_argument( + "--xsdFilepath", + type=str, + default="", + help="path to xsd file.", + required=True, + ) + parser.add_argument( + "--xmlFilepath", + type=str, + default="", + help="path to xml file.", + ) + + return parser + + +def main(args: argparse.Namespace) -> None: + XMLSchema.meta_schema.validate(args.xsdFilepath) + obj = XMLSchema.meta_schema.decode(args.xsdFilepath) + + if args.xmlFilepath: + schema = XMLSchema(args.xsdFilepath) + schema.validate(args.xmlFilepath) + + else: + print("No xml file provided") + + +def run() -> None: + parser = parsing() + args, unknown_args = parser.parse_known_args() + main(args) + + +if __name__ == "__main__": + run() diff --git a/geos-xml-viewer/src/geos_xml_viewer/bin/viewer.py b/geos-xml-viewer/src/geos_xml_viewer/bin/viewer.py new file mode 100644 index 00000000..b1966916 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/bin/viewer.py @@ -0,0 +1,871 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +import argparse +import time +from datetime import timedelta + +import colorcet as cc # type: ignore[import-untyped] +import pyvista as pv +import vtkmodules.all as vtk +from geos_xml_viewer.filters.geosDeckReader import GeosDeckReader +from geos_xml_viewer.geos.models.schema import Problem +from xsdata.formats.dataclass.context import XmlContext +from xsdata.formats.dataclass.parsers import XmlParser +from xsdata.formats.dataclass.parsers.config import ParserConfig + + +def parsing() -> argparse.ArgumentParser: + parser = argparse.ArgumentParser( + description="Extract Internal wells into VTK files" + ) + + parser.add_argument( + "-xp", + "--xmlFilepath", + type=str, + default="", + help="path to xml file.", + required=True, + ) + parser.add_argument( + "-vtpc", "--vtpcFilepath", type=str, default="", help="path to .vtpc file." + ) + parser.add_argument( + "--showmesh", + default=True, + action=argparse.BooleanOptionalAction, + help="show mesh.", + ) + parser.add_argument( + "--showsurfaces", + default=True, + action=argparse.BooleanOptionalAction, + help="show surfaces.", + ) + parser.add_argument( + "--showboxes", + default=True, + action=argparse.BooleanOptionalAction, + help="show boxes.", + ) + parser.add_argument( + "--showwells", + default=True, + action=argparse.BooleanOptionalAction, + help="show wells.", + ) + parser.add_argument( + "--showperforations", + default=True, + action=argparse.BooleanOptionalAction, + help="show well perforations.", + ) + parser.add_argument( + "--clipToBoxes", + default=True, + action=argparse.BooleanOptionalAction, + help="show only mesh elements inside boxes from xml file.", + ) + parser.add_argument( + "--Zamplification", + type=float, + default=1, + action="store", + help="Z amplification factor.", + ) + parser.add_argument( + "--attributeName", + type=str, + default="attribute", + help="Attribute name.", + required=False, + ) + + return parser + + +class WellViewer: + def __init__(self, size: float, amplification: float) -> None: + self.input: list[pv.PolyData] = [] + self.tubes: list[pv.PolyData] = [] + self.size: float = size + self.amplification: float = amplification + self.STARTING_VALUE: float = 5.0 + + def __call__(self, value: float) -> None: + self.update(value) + + def add_mesh(self, mesh: pv.PolyData) -> None: + self.input.append(mesh) # type: ignore + radius = self.size * (self.STARTING_VALUE / 100) + self.tubes.append( + mesh.tube( + radius=radius, n_sides=50 + ) # .scale([1.0, 1.0, self.amplification], inplace=True) + ) # type: ignore + + def update(self, value: float) -> None: + radius = self.size * (value / 100) + for idx, m in enumerate(self.input): + self.tubes[idx].copy_from( + m.tube( + radius=radius, n_sides=50 + ) # .scale([1.0, 1.0, self.amplification], inplace=True) + ) + + +class PerforationViewer: + def __init__(self, size: float) -> None: + self.input: list[pv.PointSet] = [] + self.spheres: list[pv.Sphere] = [] + self.size: float = size + self.STARTING_VALUE: float = 5.0 + + def __call__(self, value: float) -> None: + self.update(value) + + def add_mesh(self, mesh: pv.PointSet) -> None: + self.input.append(mesh) # type: ignore + radius: float = self.size * (self.STARTING_VALUE / 100) + self.spheres.append(pv.Sphere(center=mesh.center, radius=radius)) + + def update(self, value: float) -> None: + radius: float = self.size * (value / 100) + for idx, m in enumerate(self.input): + self.spheres[idx].copy_from(pv.Sphere(center=m.center, radius=radius)) + + +class RegionViewer: + def __init__(self) -> None: + self.input: pv.UnstructuredGrid = pv.UnstructuredGrid() + self.mesh: pv.UnstructuredGrid + + def __call__(self, normal: tuple[float], origin: tuple[float]) -> None: + self.update_clip(normal, origin) + + def add_mesh(self, mesh: pv.UnstructuredGrid) -> None: + self.input.merge(mesh, inplace=True) # type: ignore + self.mesh = self.input.copy() # type: ignore + + def update_clip(self, normal: tuple[float], origin: tuple[float]) -> None: + self.mesh.copy_from(self.input.clip(normal=normal, origin=origin, crinkle=True)) # type: ignore + + +class SetVisibilityCallback: + """Helper callback to keep a reference to the actor being modified.""" + + def __init__(self, actor: vtk.vtkActor) -> None: + self.actor = actor + + def __call__(self, state: bool) -> None: + self.actor.SetVisibility(state) + + +class SetVisibilitiesCallback: + """Helper callback to keep a reference to the actor being modified.""" + + def __init__(self) -> None: + self.actors: list[vtk.vtkActor] = [] + + def add_actor(self, actor: vtk.vtkActor) -> None: + self.actors.append(actor) + + def update_visibility(self, state: bool) -> None: + for actor in self.actors: + actor.SetVisibility(state) + + def __call__(self, state: bool) -> None: + for actor in self.actors: + actor.SetVisibility(state) + + +def find_surfaces(xmlFile: str) -> list[str]: + """Find all surfaces in xml file.""" + config = ParserConfig( + base_url=None, + load_dtd=False, + process_xinclude=False, + fail_on_unknown_properties=True, + fail_on_unknown_attributes=True, + fail_on_converter_warnings=True, + ) + + parser = XmlParser(context=XmlContext()) # , config=config) + problem = parser.parse(xmlFile, Problem) + + used: list[str] = [] + for f in problem.field_specifications: + for f2 in f.field_specification: + names = f2.set_names + names = names.replace("{", "[").replace("}", "]") + e = names.strip("][").split(",") + e = [element.strip() for element in e] + if "all" in e: + e.remove("all") + if e: + used += e + + return used + + +def main(args: argparse.Namespace) -> None: + start_time = time.monotonic() + pdsc: vtk.vtkPartitionedDataSetCollection + + if args.vtpcFilepath != "": + reader = vtk.vtkXMLPartitionedDataSetCollectionReader() + reader.SetFileName(args.vtpcFilepath) + reader.Update() + pdsc = reader.GetOutput() + else: + reader = GeosDeckReader() + reader.SetFileName(args.xmlFilepath) + reader.SetAttributeName(args.attributeName) + reader.Update() + pdsc = reader.GetOutputDataObject(0) + + read_time = time.monotonic() + print("time elapsed reading files: ", timedelta(seconds=read_time - start_time)) + + assembly: vtk.vtkDataAssembly = pdsc.GetDataAssembly() + root_name: str = assembly.GetNodeName(assembly.GetRootNode()) + surfaces_used = find_surfaces(args.xmlFilepath) + + print("surfaces used as boundary conditionsp", surfaces_used) + + global_bounds = [0, 0, 0, 0, 0, 0] + + plotter = pv.Plotter(shape=(2, 2), border=True) + ## 1. Region subview + region_engine = RegionViewer() + if args.showmesh: + start = time.monotonic() + plotter.subplot(0, 0) + + mesh = assembly.GetFirstNodeByPath("//" + root_name + "/Mesh") + + for sub_node in assembly.GetChildNodes(mesh, False): + datasets = assembly.GetDataSetIndices(sub_node, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + grid = pv.wrap(dataset.GetPartition(0)) + # grid.scale([1.0, 1.0, args.Zamplification], inplace=True) + region_engine.add_mesh(grid) + + plotter.add_mesh_clip_plane( + region_engine.mesh, + origin=region_engine.mesh.center, + normal=[-1, 0, 0], + crinkle=True, + show_edges=True, + cmap="glasbey_bw", + # cmap=cmap, + # clim=clim, + # categories=True, + scalars=args.attributeName, + # n_colors=n, + ) + stop = time.monotonic() + global_bounds = region_engine.mesh.bounds + plotter.add_text("Mesh", font_size=24) + plotter.background_color = "white" + plotter.show_bounds( + grid="back", + location="outer", + ticks="both", + n_xlabels=2, + n_ylabels=2, + n_zlabels=2, + ztitle="Elevation", + use_3d_text=True, + minor_ticks=True, + ) + print("region subplot preparation time: ", timedelta(seconds=stop - start)) + + # 2. Surfaces subview + if args.showsurfaces: + start = time.monotonic() + plotter.subplot(0, 1) + + surfaces = assembly.GetFirstNodeByPath("//" + root_name + "/Surfaces") + + if surfaces > 0: + Startpos = 12 + size = 35 + for i, sub_node in enumerate(assembly.GetChildNodes(surfaces, False)): + datasets = assembly.GetDataSetIndices(sub_node, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + label = assembly.GetAttributeOrDefault( + sub_node, "label", "no label" + ) + matches = ["Surface" + s for s in surfaces_used] + if any(x in label for x in matches): + actor = plotter.add_mesh( + pv.wrap( + dataset.GetPartition(0) + ), # .scale([1.0, 1.0, args.Zamplification], inplace=True), + show_edges=True, + color=cc.cm.glasbey_bw(i), # type: ignore + ) + callback = SetVisibilityCallback(actor) + plotter.add_checkbox_button_widget( + callback, + value=True, + position=(Startpos, 10.0), + size=size, + border_size=1, + color_on=cc.cm.glasbey_bw(i), + color_off=cc.cm.glasbey_bw(i), + background_color="grey", + ) + Startpos = Startpos + size + (size // 10) + else: + actor = plotter.add_mesh( + pv.wrap( + dataset.GetPartition(0) + ), # .scale([1.0, 1.0, args.Zamplification], inplace=True), + show_edges=True, + color=cc.cm.glasbey_bw(i), # type: ignore + opacity=0.2, + ) + callback = SetVisibilityCallback(actor) + plotter.add_checkbox_button_widget( + callback, + value=True, + position=(Startpos, 10.0), + size=size, + border_size=1, + color_on=cc.cm.glasbey_bw(i), + color_off=cc.cm.glasbey_bw(i), + background_color="grey", + ) + Startpos = Startpos + size + (size // 10) + + plotter.add_text("Surfaces", font_size=24) + plotter.show_bounds( + bounds=global_bounds, + grid="back", + location="outer", + ticks="both", + n_xlabels=2, + n_ylabels=2, + n_zlabels=2, + ztitle="Elevation", + minor_ticks=True, + ) + + stop = time.monotonic() + + print("surfaces subplot preparation time: ", timedelta(seconds=stop - start)) + + # 3. Well subview + if args.showwells: + start = time.monotonic() + plotter.subplot(1, 0) + + bounds = global_bounds + xsize = bounds[1] - bounds[0] + ysize = bounds[3] - bounds[2] + + maxsize = max(xsize, ysize) + + well_engine = WellViewer(maxsize, args.Zamplification) + perfo_engine = PerforationViewer(maxsize) + + wells = assembly.GetFirstNodeByPath("//" + root_name + "/Wells") + if wells > 0: + for well in assembly.GetChildNodes(wells, False): + sub_nodes = assembly.GetChildNodes(well, False) + for sub_node in sub_nodes: + if assembly.GetNodeName(sub_node) == "Mesh": + datasets = assembly.GetDataSetIndices(sub_node, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + if dataset.GetPartition(0) is not None: + well_engine.add_mesh( + pv.wrap(dataset.GetPartition(0)) + ) # .scale([1.0, 1.0, args.Zamplification], inplace=True)) # + elif assembly.GetNodeName(sub_node) == "Perforations": + for i, perfos in enumerate( + assembly.GetChildNodes(sub_node, False) + ): + datasets = assembly.GetDataSetIndices(perfos, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + if dataset.GetPartition(0) is not None: + pointset = pv.wrap( + dataset.GetPartition(0) + ) # .cast_to_pointset().scale([1.0, 1.0, args.Zamplification], inplace=True) # + perfo_engine.add_mesh(pointset) + + plotter.add_slider_widget( + callback=well_engine.update, rng=[0.1, 10], title="Wells Radius" + ) + + well_visibilty: SetVisibilitiesCallback = SetVisibilitiesCallback() + for m in well_engine.tubes: + actor = plotter.add_mesh(m, color=True, show_edges=False) + well_visibilty.add_actor(actor) + + size = 35 + plotter.add_checkbox_button_widget( + callback=well_visibilty.update_visibility, + value=True, + position=(50, 10.0), + size=size, + border_size=1, + ) + + my_cell_locator = vtk.vtkStaticCellLocator() + my_cell_locator.SetDataSet(region_engine.input) + my_cell_locator.AutomaticOn() + my_cell_locator.SetNumberOfCellsPerNode(20) + + my_cell_locator.BuildLocator() + + if len(perfo_engine.spheres) > 0: + Startpos = 12 + callback: SetVisibilitiesCallback = SetVisibilitiesCallback() + for m in perfo_engine.spheres: + actor = plotter.add_mesh(m, color=True, show_edges=False) + callback.add_actor(actor) + # render cell containing perforation + cell_id = my_cell_locator.FindCell(m.center) + if cell_id != -1: + id_list = vtk.vtkIdList() + id_list.InsertNextId(cell_id) + extract = vtk.vtkExtractCells() + extract.SetInputDataObject(region_engine.input) + extract.SetCellList(id_list) + extract.Update() + cell = extract.GetOutputDataObject(0) + + # cell = region_engine.input.extract_cells(cell_id) # type: ignore + plotter.add_mesh( + pv.wrap(cell).scale( + [1.0, 1.0, args.Zamplification], inplace=True + ), + opacity=0.5, + color="red", + smooth_shading=True, + show_edges=True, + ) + + plotter.add_checkbox_button_widget( + callback=callback.update_visibility, + value=True, + position=(Startpos, 10.0), + size=size, + border_size=1, + ) + + plotter.add_slider_widget( + callback=perfo_engine.update, + starting_value=perfo_engine.STARTING_VALUE, + rng=[0.1, 10], + title=" Perforations\n Radius", + pointb=(0.08, 0.9), + pointa=(0.08, 0.03), + # title_height=0.03 + ) + + plotter.add_text("Wells", font_size=24) + plotter.show_bounds( + bounds=global_bounds, + grid="back", + location="outer", + ticks="both", + n_xlabels=2, + n_ylabels=2, + n_zlabels=2, + ztitle="Elevation", + minor_ticks=True, + ) + stop = time.monotonic() + print("wells subplot preparation time: ", timedelta(seconds=stop - start)) + + ## 5. Box subview + if args.showboxes: + start = time.monotonic() + plotter.subplot(1, 1) + + boxes = assembly.GetFirstNodeByPath("//" + root_name + "/Boxes") + + if boxes > 0: + for i, sub_node in enumerate(assembly.GetChildNodes(boxes, False)): + datasets = assembly.GetDataSetIndices(sub_node, False) + for d in datasets: + dataset = pdsc.GetPartitionedDataSet(d) + plotter.add_mesh( + pv.wrap( + dataset.GetPartition(0) + ), # .scale([1.0, 1.0, args.Zamplification], inplace=True), + color="red", + show_edges=True, # type: ignore + ) + + plotter.add_text("Boxes", font_size=24) + plotter.show_bounds( + bounds=global_bounds, + grid="back", + location="outer", + ticks="both", + n_xlabels=2, + n_ylabels=2, + n_zlabels=2, + ztitle="Elevation", + minor_ticks=True, + ) + + stop = time.monotonic() + print("boxes subplot preparation time: ", timedelta(seconds=stop - start)) + + show_time = time.monotonic() + print("time elapsed showing data: ", timedelta(seconds=show_time - read_time)) + + plotter.link_views(0) # link all the views + plotter.show() + + +def run() -> None: + parser = parsing() + args, unknown_args = parser.parse_known_args() + main(args) + + +if __name__ == "__main__": + run() + + +# def get_data_element_index( +# assembly: vtk.vtkDataAssembly, name: str +# ) -> list[vtk.vtkIdType] | None : +# node_id = assembly.FindFirstNodeWithName(name) +# if node_id == -1: +# return None +# ds_indices = assembly.GetDataSetIndices(node_id) + +# return ds_indices + + +# class MyCustomRoutine: +# def __init__(self, mesh): +# self.input = mesh +# self.mesh = mesh.copy() # Expected PyVista mesh type + +# # default parameters +# self.kwargs = {} + +# self._last_normal = "z" +# self._last_origin = self.mesh.center + +# def __call__(self, param, value): +# self.kwargs[param] = value +# self.update() + +# def update(self) -> None: +# self.update_clip(self._last_normal, self._last_origin) +# return + +# def update_clip(self, normal, origin): +# self.mesh.copy_from(self.input.clip(normal=normal, origin=origin, crinkle=True)) +# self._last_normal = normal +# self._last_origin = origin + + +# def distinct_colors( +# start: int = 0, stop: int = 20, sat_values=[8 / 10] +# ): # -> np.NDArray[np.float64] +# """Returns an array of distinct RGB colors, from an infinite sequence of colors""" +# if stop <= start: # empty interval; return empty array +# return np.array([], dtype=np.float64) +# # sat_values = # other tones could be added +# val_values = [8 / 10, 5 / 10] # other tones could be added +# colors_per_hue_value = len(sat_values) * len(val_values) +# # Get the start and stop indices within the hue value stream that are needed +# # to achieve the requested range +# hstart = start // colors_per_hue_value +# hstop = (stop + colors_per_hue_value - 1) // colors_per_hue_value +# # Zero will cause a singularity in the caluculation, so we will add the zero +# # afterwards +# prepend_zero = hstart == 0 + +# # Sequence (if hstart=1): 1,2,...,hstop-1 +# i = np.arange(1 if prepend_zero else hstart, hstop) +# # The following yields (if hstart is 1): 1/2, 1/4, 3/4, 1/8, 3/8, 5/8, 7/8, +# # 1/16, 3/16, ... +# hue_values = (2 * i + 1) / np.power(2, np.floor(np.log2(i * 2))) - 1 + +# if prepend_zero: +# hue_values = np.concatenate(([0], hue_values)) + +# # Make all combinations of h, s and v values, as if done by a nested loop +# # in that order +# hsv = ( +# np.array(np.meshgrid(hue_values, sat_values, val_values, indexing="ij")) +# .reshape((3, -1)) +# .transpose() +# ) + +# # Select the requested range (only the necessary values were computed but we +# # need to adjust the indices since start & stop are not necessarily multiples +# # of colors_per_hue_value) +# hsv = hsv[ +# start % colors_per_hue_value : start % colors_per_hue_value + stop - start +# ] +# # Use the matplotlib vectorized function to convert hsv to rgb +# return mplt.colors.hsv_to_rgb(hsv) + + +# def mainOLD(args: argparse.Namespace) -> None: + +# start_time = time.monotonic() +# pdsc: vtk.vtkPartitionedDataSetCollection + +# if(args.vtpcFilepath != ""): +# reader = vtk.vtkXMLPartitionedDataSetCollectionReader() +# reader.SetFileName(args.vtpcFilepath) +# reader.Update() +# pdsc: vtk.vtkPartitionedDataSetCollection = reader.GetOutput() + +# else: +# reader = GeosDeckReader() +# reader.SetFileName(args.xmlFilepath) +# reader.SetAttributeName(args.attributeName) +# reader.Update() +# pdsc: vtk.vtkPartitionedDataSetCollection = reader.GetOutputDataObject(0) + +# config = ParserConfig( +# base_url=None, +# load_dtd=False, +# process_xinclude=False, +# fail_on_unknown_properties=True, +# fail_on_unknown_attributes=True, +# fail_on_converter_warnings=True, +# ) + +# parser = XmlParser(context=XmlContext()) #, config=config) +# problem = parser.parse(args.xmlFilepath, Problem) + +# for e in problem.events: +# # for pe in e.periodic_event: +# print(type(e.max_time), e.max_time) + + +# used = [] +# for f in problem.field_specifications: +# for f2 in f.field_specification: +# names = f2.set_names +# names = names.replace('{','[').replace('}',']') +# # print(names) +# # print(ast.literal_eval(names)) +# # json.loads(names) +# e = [i.split('}')[0].strip() for i in f2.set_names.split('{')[1:]] +# if 'all' in e: e.remove('all') +# if e: +# print(e) +# used += e + +# print(used) + +# read_time = time.monotonic() +# print("time elapsed reading files: ", timedelta(seconds=read_time - start_time)) + + +# plotter = pv.Plotter(shape=(2, 2), border=True) +# plotter.background_color = "white" + +# engine = RegionViewer() + +# n = pdsc.GetNumberOfPartitionedDataSets() +# dark_color_map = ListedColormap(distinct_colors(stop=n)) +# light_color_map = ListedColormap(distinct_colors(stop=n, sat_values=[3/10])) + +# c = 0.3 +# test = [ +# mplt.colors.rgb_to_hsv(mplt.colors.to_rgb(x)) +# for x in cc.cm.glasbey_bw(np.linspace(0.0, 1.0, n)) +# ] +# pastel_glasbey = colors = (1.0 - c) * cc.cm.glasbey_bw( +# np.linspace(0.0, 1.0, n) +# ) + c * np.ones((n, 4)) +# colors = np.stack(test) +# print(colors) +# pastel_glasbey = mplt.colors.rgb_to_hsv(test) +# colors[:,1]+=0.1 +# colors[:,1]-=0.1 +# print(colors) +# pastel_glasbey = mplt.colors.hsv_to_rgb(colors) +# pastel_glasbey = [mplt.colors.to_rgba(mplt.colors.hsv_to_rgb(x)) for x in colors] +# print(pastel_glasbey) +# print(type(cc.cm.glasbey_bw)) + +# print(n) +# color_map = pv.LookupTable('glasbey_bw', n_values=n) + +# data_assembly = pdsc.GetDataAssembly() +# regions = assembly.SelectNodes("//box_hybrid_fault_0-01/Region4") +# print(regions) +# regions = assembly.SelectNodes('//Mesh/Region4') +# print(regions) + +# perfos = [] + +# Startpos = 12 +# size = 35 +# for i in range(pdsc.GetNumberOfPartitionedDataSets()): +# psm = pdsc.GetPartitionedDataSet(i) +# name = pdsc.GetMetaData(i).Get(vtk.vtkCompositeDataSet.NAME()) +# if name.startswith("Region") and args.showmesh: +# stime = time.monotonic() +# engine.add_mesh(pv.wrap(psm.GetPartition(0))) # type: ignore +# etime = time.monotonic() +# print("time building region view: ", timedelta(seconds=etime - stime)) +# elif name.startswith("Surface") and args.showsurfaces: +# stime = time.monotonic() +# # "Surface"+used[0] in name: +# # matches = ["Surface" + s for s in used] +# # if any(x in name for x in matches): +# plotter.subplot(0, 1) +# actor = plotter.add_mesh( +# pv.wrap(psm.GetPartition(0)), +# show_edges=True, +# color=cc.cm.glasbey_bw(i), # type: ignore +# ) +# callback = SetVisibilityCallback(actor) +# plotter.add_checkbox_button_widget( +# callback, +# value=True, +# position=(Startpos, 10.0), +# size=size, +# border_size=1, +# color_on=cc.cm.glasbey_bw(i), +# color_off=cc.cm.glasbey_bw(i), +# background_color="grey", +# ) +# Startpos = Startpos + size + (size // 10) +# else: +# plotter.subplot(0, 1) +# actor = plotter.add_mesh( +# pv.wrap(psm.GetPartition(0)), +# show_edges=True, +# color=cc.cm.glasbey_bw(i), # type: ignore +# opacity=0.2 +# ) +# callback = SetVisibilityCallback(actor) +# plotter.add_checkbox_button_widget( +# callback, +# value=True, +# position=(Startpos, 10.0), +# size=size, +# border_size=1, +# color_on=cc.cm.glasbey_bw(i), +# color_off=cc.cm.glasbey_bw(i), +# background_color="grey", +# ) +# Startpos = Startpos + size + (size // 10) +# etime = time.monotonic() +# print("time building region view: ", timedelta(seconds=etime - stime)) +# elif name.startswith("Well") and args.showwells: +# plotter.subplot(1, 0) +# plotter.add_mesh( +# pv.wrap(psm.GetPartition(0)).tube(radius=0.025, n_sides=50), # type: ignore +# color=True, +# show_edges=False, +# ) +# elif name.startswith("Perforation") and args.showperforations: +# plotter.subplot(1, 0) +# plotter.add_mesh(pv.wrap(psm.GetPartition(0)), color=True, show_edges=False) # type: ignore +# perfos.append(pv.wrap(psm.GetPartition(0))) # type: ignore +# elif name.startswith("Box") and args.showboxes: +# plotter.subplot(1, 1) +# plotter.add_mesh( +# pv.wrap(psm.GetPartition(0)), +# color="red", +# show_edges=True, # type: ignore +# ) # , style="wireframe") + +# extracted = engine.input.clip_box( # type: ignore +# bounds=pv.wrap(psm.GetPartition(0)).bounds, +# invert=False, +# crinkle=True, # type: ignore +# ) + +# recuperer le tableau extracted['cell_ids'] +# dans le maillage d'entree faire +10 a l'attribut de ces cellules + +# exploded = extracted.explode(0.1) +# # plotter.add_mesh(b.mesh, opacity=0.5, color="red") +# plotter.add_mesh( +# exploded, +# show_edges=True, +# smooth_shading=True, +# # color="green", +# cmap="glasbey_bw", +# opacity=1.00, +# ) + +# plotter.subplot(0, 0) +# plotter.add_text("Mesh", font_size=24) +# # plotter.set_scale(zscale=args.Zamplification) +# plotter.show_axes() + +# plotter.add_mesh_clip_plane( +# engine.mesh, +# origin=engine.mesh.center, +# normal=[-1, 0, 0], +# crinkle=True, +# show_edges=True, +# cmap="glasbey_bw", +# # cmap=cmap, +# # clim=clim, +# # categories=True, +# scalars=args.attributeName, +# # n_colors=n, +# ) + + +# plotter.subplot(1, 0) +# plotter.add_text("Wells", font_size=24) +# # plotter.set_scale(zscale=args.Zamplification) +# plotter.add_mesh(engine.input, opacity=0.1) +# plotter.show_bounds( +# grid="back", +# location="outer", +# ticks="both", +# n_xlabels=2, +# n_ylabels=2, +# n_zlabels=2, +# ztitle="Elevation", +# ) +# plotter.show_axes() + +# my_cell_locator = vtk.vtkCellLocator() +# my_cell_locator.SetDataSet(engine.input) + +# for p in perfos: +# cell_id = my_cell_locator.FindCell(p.points[0]) +# cell = engine.input.extract_cells(cell_id) # type: ignore +# plotter.add_mesh( +# cell, opacity=0.5, color="red", smooth_shading=True, show_edges=True +# ) + +# plotter.subplot(1, 1) +# plotter.add_text("Boxes", font_size=24) +# # plotter.set_scale(zscale=args.Zamplification) +# plotter.add_mesh(engine.input, opacity=0.1) +# plotter.show_axes() + +# plotter.link_views() # link all the views + +# plotter.show_grid() + +# show_time = time.monotonic() +# print("time elapsed showing data: ", timedelta(seconds=show_time - read_time)) + +# plotter.show(auto_close=False) +# image = plotter.screenshot('test.png', return_img=True) +# plotter.close() diff --git a/geos-xml-viewer/src/geos_xml_viewer/filters/__init__.py b/geos-xml-viewer/src/geos_xml_viewer/filters/__init__.py new file mode 100644 index 00000000..ffa33702 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/filters/__init__.py @@ -0,0 +1,4 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + diff --git a/geos-xml-viewer/src/geos_xml_viewer/filters/geosDeckReader.py b/geos-xml-viewer/src/geos_xml_viewer/filters/geosDeckReader.py new file mode 100644 index 00000000..bd53f2fa --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/filters/geosDeckReader.py @@ -0,0 +1,77 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner +from typing_extensions import Self + +import vtkmodules.all as vtk +from vtkmodules.util.vtkAlgorithm import VTKPythonAlgorithmBase + +from geos_xml_viewer.algorithms.deck import SimulationDeck, build_model, read + + +class GeosDeckReader(VTKPythonAlgorithmBase): + def __init__(self: Self) -> Self: + """VTK GEOS deck reader filter.""" + VTKPythonAlgorithmBase.__init__( + self, + nInputPorts=0, + nOutputPorts=1, + outputType="vtkPartitionedDataSetCollection", + ) # type: ignore + self.__filename: str = "" + self.__attributeName: str = "" + self.__simulationDeck: SimulationDeck + + def SetFileName(self: Self, name: str) -> None: + """Set the filename. + + Args: + name (str): filename + """ + if name != self.__filename: + self.__filename = name + self.Modified() + + def GetFileName(self: Self) -> str: + """Get the filename.""" + return self.__filename + + def SetAttributeName(self: Self, name: str) -> None: + """Set the attribute name. + + Args: + name (str): attribute name + """ + if name != self.__attributeName: + self.__attributeName = name + self.Modified() + + def GetAttributeName(self: Self) -> str: + """Get the attribute name.""" + return self.__attributeName + + def RequestData( + self: Self, + request: vtk.vtkInformation, + inInfoVec: vtk.vtkInformationVector, + outInfoVec: vtk.vtkInformationVector, + ) -> int: + """RequestData function of the vtk pipeline. + + Args: + request (vtkInformation): information about the request + inInfoVec (vtkInformationVector): input information vector + outInfoVec (vtkInformationVector): output information vector + + Returns: + int: Returns 1 if the pipeline is successful + """ + self.__simulationDeck = read(self.__filename) + opt = vtk.vtkPartitionedDataSetCollection.GetData(outInfoVec) + + output = vtk.vtkPartitionedDataSetCollection() + build_model(self.__simulationDeck, output, self.__attributeName) + + opt.ShallowCopy(output) + + return 1 diff --git a/geos-xml-viewer/src/geos_xml_viewer/geos/__init__.py b/geos-xml-viewer/src/geos_xml_viewer/geos/__init__.py new file mode 100644 index 00000000..361de238 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/geos/__init__.py @@ -0,0 +1,6 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + + +# nothing here diff --git a/geos-xml-viewer/src/geos_xml_viewer/geos/models/__init__.py b/geos-xml-viewer/src/geos_xml_viewer/geos/models/__init__.py new file mode 100644 index 00000000..9461369b --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/geos/models/__init__.py @@ -0,0 +1,395 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +from geos_xml_viewer.geos.models.schema import ( + AcousticFirstOrderSemtype, + AcousticSemtype, + AcousticVtisemtype, + AquiferType, + BenchmarksType, + BiotPorosityType, + BlackOilFluidType, + BlueprintType, + BoxType, + BrooksCoreyBakerRelativePermeabilityType, + BrooksCoreyCapillaryPressureType, + BrooksCoreyRelativePermeabilityType, + BrooksCoreyStone2RelativePermeabilityType, + CarmanKozenyPermeabilityType, + CellElementRegionType, + CeramicDamageType, + ChomboIotype, + Co2BrineEzrokhiFluidType, + Co2BrineEzrokhiThermalFluidType, + Co2BrinePhillipsFluidType, + Co2BrinePhillipsThermalFluidType, + CompositeFunctionType, + CompositionalMultiphaseFluidType, + CompositionalMultiphaseFvmtype, + CompositionalMultiphaseHybridFvmtype, + CompositionalMultiphaseReservoirPoromechanicsInitializationType, + CompositionalMultiphaseReservoirPoromechanicsType, + CompositionalMultiphaseReservoirType, + CompositionalMultiphaseStatisticsType, + CompositionalMultiphaseWellType, + CompositonalTwoPhaseFluidPengRobinsonType, + CompositonalTwoPhaseFluidSoaveRedlichKwongType, + CompressibleSinglePhaseFluidType, + CompressibleSolidCarmanKozenyPermeabilityType, + CompressibleSolidConstantPermeabilityType, + CompressibleSolidExponentialDecayPermeabilityType, + CompressibleSolidParallelPlatesPermeabilityType, + CompressibleSolidSlipDependentPermeabilityType, + CompressibleSolidWillisRichardsPermeabilityType, + ConstantDiffusionType, + ConstantPermeabilityType, + ConstitutiveType, + CoulombType, + CrusherType, + CustomPolarObjectType, + CylinderType, + DamageElasticIsotropicType, + DamageSpectralElasticIsotropicType, + DamageVolDevElasticIsotropicType, + DeadOilFluidType, + DelftEggType, + DirichletType, + DiscType, + DruckerPragerType, + ElasticFirstOrderSemtype, + ElasticIsotropicPressureDependentType, + ElasticIsotropicType, + ElasticOrthotropicType, + ElasticSemtype, + ElasticTransverseIsotropicType, + ElementRegionsType, + EmbeddedSurfaceGeneratorType, + EventsType, + ExponentialDecayPermeabilityType, + ExtendedDruckerPragerType, + FieldSpecificationsType, + FieldSpecificationType, + FileType, + FiniteElementSpaceType, + FiniteElementsType, + FiniteVolumeType, + FlowProppantTransportType, + FrictionlessContactType, + FunctionsType, + GeometryType, + HaltEventType, + HybridMimeticDiscretizationType, + HydrofractureType, + HydrostaticEquilibriumType, + IncludedType, + InternalMeshType, + InternalWellboreType, + InternalWellType, + JfunctionCapillaryPressureType, + LagrangianContactType, + LaplaceFemtype, + LassenType, + LinearIsotropicDispersionType, + LinearSolverParametersType, + MeshType, + ModifiedCamClayType, + MultiPhaseConstantThermalConductivityType, + MultiphasePoromechanicsInitializationType, + MultiphasePoromechanicsReservoirType, + MultiphasePoromechanicsType, + MultiPhaseVolumeWeightedThermalConductivityType, + MultivariableTableFunctionType, + NonlinearSolverParametersType, + NullModelType, + NumericalMethodsType, + OutputsType, + PackCollectionType, + ParallelPlatesPermeabilityType, + ParametersType, + ParameterType, + ParticleFluidType, + ParticleMeshType, + ParticleRegionsType, + ParticleRegionType, + PerfectlyPlasticType, + PerforationType, + PeriodicEventType, + PermeabilityBaseType, + PhaseFieldDamageFemtype, + PhaseFieldFractureType, + Pmltype, + PorousDelftEggType, + PorousDruckerPragerType, + PorousElasticIsotropicType, + PorousElasticOrthotropicType, + PorousElasticTransverseIsotropicType, + PorousExtendedDruckerPragerType, + PorousModifiedCamClayType, + PressurePorosityType, + Problem, + ProblemType, + ProppantPermeabilityType, + ProppantPorosityType, + ProppantSlurryFluidType, + ProppantSolidProppantPermeabilityType, + ProppantTransportType, + PvtdriverType, + PythonType, + QuartzType, + ReactiveBrineThermalType, + ReactiveBrineType, + ReactiveCompositionalMultiphaseObltype, + ReactiveFluidDriverType, + RectangleType, + RelpermDriverType, + RestartType, + RunType, + SiloType, + SinglePhaseConstantThermalConductivityType, + SinglePhaseFvmtype, + SinglePhaseHybridFvmtype, + SinglePhasePoromechanicsConformingFracturesType, + SinglePhasePoromechanicsEmbeddedFracturesType, + SinglePhasePoromechanicsInitializationType, + SinglePhasePoromechanicsReservoirType, + SinglePhasePoromechanicsType, + SinglePhaseProppantFvmtype, + SinglePhaseReservoirPoromechanicsInitializationType, + SinglePhaseReservoirPoromechanicsType, + SinglePhaseReservoirType, + SinglePhaseStatisticsType, + SinglePhaseWellType, + SlipDependentPermeabilityType, + SolidInternalEnergyType, + SolidMechanicsEmbeddedFracturesType, + SolidMechanicsLagrangianFemtype, + SolidMechanicsLagrangianSsletype, + SolidMechanicsMpmtype, + SolidMechanicsStateResetType, + SolidMechanicsStatisticsType, + SoloEventType, + SolversType, + SourceFluxType, + SurfaceElementRegionType, + SurfaceGeneratorType, + SymbolicFunctionType, + TableCapillaryPressureType, + TableFunctionType, + TableRelativePermeabilityHysteresisType, + TableRelativePermeabilityType, + TasksType, + ThermalCompressibleSinglePhaseFluidType, + ThickPlaneType, + TimeHistoryType, + TractionType, + TriaxialDriverType, + TwoPointFluxApproximationType, + VanGenuchtenBakerRelativePermeabilityType, + VanGenuchtenCapillaryPressureType, + VanGenuchtenStone2RelativePermeabilityType, + ViscoDruckerPragerType, + ViscoExtendedDruckerPragerType, + ViscoModifiedCamClayType, + VtkmeshType, + Vtktype, + WellControlsType, + WellElementRegionType, + WillisRichardsPermeabilityType, +) + +__all__ = [ + "AcousticFirstOrderSemtype", + "AcousticSemtype", + "AcousticVtisemtype", + "AquiferType", + "BenchmarksType", + "BiotPorosityType", + "BlackOilFluidType", + "BlueprintType", + "BoxType", + "BrooksCoreyBakerRelativePermeabilityType", + "BrooksCoreyCapillaryPressureType", + "BrooksCoreyRelativePermeabilityType", + "BrooksCoreyStone2RelativePermeabilityType", + "Co2BrineEzrokhiFluidType", + "Co2BrineEzrokhiThermalFluidType", + "Co2BrinePhillipsFluidType", + "Co2BrinePhillipsThermalFluidType", + "CarmanKozenyPermeabilityType", + "CellElementRegionType", + "CeramicDamageType", + "ChomboIotype", + "CompositeFunctionType", + "CompositionalMultiphaseFvmtype", + "CompositionalMultiphaseFluidType", + "CompositionalMultiphaseHybridFvmtype", + "CompositionalMultiphaseReservoirPoromechanicsInitializationType", + "CompositionalMultiphaseReservoirPoromechanicsType", + "CompositionalMultiphaseReservoirType", + "CompositionalMultiphaseStatisticsType", + "CompositionalMultiphaseWellType", + "CompositonalTwoPhaseFluidPengRobinsonType", + "CompositonalTwoPhaseFluidSoaveRedlichKwongType", + "CompressibleSinglePhaseFluidType", + "CompressibleSolidCarmanKozenyPermeabilityType", + "CompressibleSolidConstantPermeabilityType", + "CompressibleSolidExponentialDecayPermeabilityType", + "CompressibleSolidParallelPlatesPermeabilityType", + "CompressibleSolidSlipDependentPermeabilityType", + "CompressibleSolidWillisRichardsPermeabilityType", + "ConstantDiffusionType", + "ConstantPermeabilityType", + "ConstitutiveType", + "CoulombType", + "CustomPolarObjectType", + "CylinderType", + "DamageElasticIsotropicType", + "DamageSpectralElasticIsotropicType", + "DamageVolDevElasticIsotropicType", + "DeadOilFluidType", + "DelftEggType", + "DirichletType", + "DiscType", + "DruckerPragerType", + "ElasticFirstOrderSemtype", + "ElasticIsotropicPressureDependentType", + "ElasticIsotropicType", + "ElasticOrthotropicType", + "ElasticSemtype", + "ElasticTransverseIsotropicType", + "ElementRegionsType", + "EmbeddedSurfaceGeneratorType", + "EventsType", + "ExponentialDecayPermeabilityType", + "ExtendedDruckerPragerType", + "FieldSpecificationType", + "FieldSpecificationsType", + "FileType", + "FiniteElementSpaceType", + "FiniteElementsType", + "FiniteVolumeType", + "FlowProppantTransportType", + "FrictionlessContactType", + "FunctionsType", + "GeometryType", + "HaltEventType", + "HybridMimeticDiscretizationType", + "HydrofractureType", + "HydrostaticEquilibriumType", + "IncludedType", + "InternalMeshType", + "InternalWellType", + "InternalWellboreType", + "JfunctionCapillaryPressureType", + "LagrangianContactType", + "LaplaceFemtype", + "LinearIsotropicDispersionType", + "LinearSolverParametersType", + "MeshType", + "ModifiedCamClayType", + "MultiPhaseConstantThermalConductivityType", + "MultiPhaseVolumeWeightedThermalConductivityType", + "MultiphasePoromechanicsInitializationType", + "MultiphasePoromechanicsReservoirType", + "MultiphasePoromechanicsType", + "MultivariableTableFunctionType", + "NonlinearSolverParametersType", + "NullModelType", + "NumericalMethodsType", + "OutputsType", + "Pmltype", + "PvtdriverType", + "PackCollectionType", + "ParallelPlatesPermeabilityType", + "ParameterType", + "ParametersType", + "ParticleFluidType", + "ParticleMeshType", + "ParticleRegionType", + "ParticleRegionsType", + "PerfectlyPlasticType", + "PerforationType", + "PeriodicEventType", + "PermeabilityBaseType", + "PhaseFieldDamageFemtype", + "PhaseFieldFractureType", + "PorousDelftEggType", + "PorousDruckerPragerType", + "PorousElasticIsotropicType", + "PorousElasticOrthotropicType", + "PorousElasticTransverseIsotropicType", + "PorousExtendedDruckerPragerType", + "PorousModifiedCamClayType", + "PressurePorosityType", + "Problem", + "ProblemType", + "ProppantPermeabilityType", + "ProppantPorosityType", + "ProppantSlurryFluidType", + "ProppantSolidProppantPermeabilityType", + "ProppantTransportType", + "PythonType", + "ReactiveBrineThermalType", + "ReactiveBrineType", + "ReactiveCompositionalMultiphaseObltype", + "ReactiveFluidDriverType", + "RectangleType", + "RelpermDriverType", + "RestartType", + "RunType", + "SiloType", + "SinglePhaseConstantThermalConductivityType", + "SinglePhaseFvmtype", + "SinglePhaseHybridFvmtype", + "SinglePhasePoromechanicsConformingFracturesType", + "SinglePhasePoromechanicsEmbeddedFracturesType", + "SinglePhasePoromechanicsInitializationType", + "SinglePhasePoromechanicsReservoirType", + "SinglePhasePoromechanicsType", + "SinglePhaseProppantFvmtype", + "SinglePhaseReservoirPoromechanicsInitializationType", + "SinglePhaseReservoirPoromechanicsType", + "SinglePhaseReservoirType", + "SinglePhaseStatisticsType", + "SinglePhaseWellType", + "SlipDependentPermeabilityType", + "SolidInternalEnergyType", + "SolidMechanicsEmbeddedFracturesType", + "SolidMechanicsLagrangianSsletype", + "SolidMechanicsStateResetType", + "SolidMechanicsStatisticsType", + "SolidMechanicsLagrangianFemtype", + "SolidMechanicsMpmtype", + "SoloEventType", + "SolversType", + "SourceFluxType", + "SurfaceElementRegionType", + "SurfaceGeneratorType", + "SymbolicFunctionType", + "TableCapillaryPressureType", + "TableFunctionType", + "TableRelativePermeabilityHysteresisType", + "TableRelativePermeabilityType", + "TasksType", + "ThermalCompressibleSinglePhaseFluidType", + "ThickPlaneType", + "TimeHistoryType", + "TractionType", + "TriaxialDriverType", + "TwoPointFluxApproximationType", + "VtkmeshType", + "Vtktype", + "VanGenuchtenBakerRelativePermeabilityType", + "VanGenuchtenCapillaryPressureType", + "VanGenuchtenStone2RelativePermeabilityType", + "ViscoDruckerPragerType", + "ViscoExtendedDruckerPragerType", + "ViscoModifiedCamClayType", + "WellControlsType", + "WellElementRegionType", + "WillisRichardsPermeabilityType", + "CrusherType", + "LassenType", + "QuartzType", +] diff --git a/geos-xml-viewer/src/geos_xml_viewer/geos/models/schema.py b/geos-xml-viewer/src/geos_xml_viewer/geos/models/schema.py new file mode 100644 index 00000000..a108a81c --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/geos/models/schema.py @@ -0,0 +1,15841 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +from dataclasses import dataclass, field +from typing import Optional + +import numpy as np +from xsdata.formats.converter import Converter, converter + + +@dataclass +class integer: + value: np.int32 + + +class integerConverter(Converter): + def deserialize(self, value: str, **kwargs) -> integer: + return integer(value) + + def serialize(self, value: integer, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(integer, integerConverter()) + + +@dataclass +class real32: + value: np.float32 + + +class real32Converter(Converter): + def deserialize(self, value: str, **kwargs) -> real32: + return real32(value) + + def serialize(self, value: real32, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(real32, real32Converter()) + + +@dataclass +class real64: + value: np.float64 = field(metadata={"decoder": np.float64}) + + +class real64Converter(Converter): + def deserialize(self, value: str, **kwargs) -> real64: + return real64(value=np.float64(value)) + + def serialize(self, value: real64, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(real64, real64Converter()) + + +@dataclass +class globalIndex: + value: np.int64 + + +class globalIndexConverter(Converter): + def deserialize(self, value: str, **kwargs) -> globalIndex: + return globalIndex(value) + + def serialize(self, value: globalIndex, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(globalIndex, globalIndexConverter()) + + +def custom_class_factory(clazz, params): + if clazz is real64: + return clazz(**{k: v for k, v in params.items()}) + + return clazz(**params) + + +# @dataclass +# class globalIndex_array: +# value: np.ndarray[np.int64] + +# class globalIndex_arrayConverter(Converter): +# def deserialize(self, value: str, **kwargs) -> globalIndex_array: +# return globalIndex_array(value) + +# def serialize(self, value: globalIndex_array, **kwargs) -> str: +# if kwargs["format"]: +# return kwargs["format"].format(value) +# return str(value) + + +@dataclass +class AquiferType: + allow_all_phases_into_aquifer: str = field( + default="0", + metadata={ + "name": "allowAllPhasesIntoAquifer", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + aquifer_angle: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferAngle", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_elevation: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_initial_pressure: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferInitialPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_inner_radius: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferInnerRadius", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_permeability: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_porosity: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferPorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_thickness: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferThickness", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_total_compressibility: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferTotalCompressibility", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_water_density: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferWaterDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + aquifer_water_phase_component_fraction: str = field( + default="{0}", + metadata={ + "name": "aquiferWaterPhaseComponentFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + aquifer_water_phase_component_names: str = field( + default="{}", + metadata={ + "name": "aquiferWaterPhaseComponentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + aquifer_water_viscosity: Optional[str] = field( + default=None, + metadata={ + "name": "aquiferWaterViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + pressure_influence_function_name: Optional[str] = field( + default=None, + metadata={ + "name": "pressureInfluenceFunctionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: Optional[str] = field( + default=None, + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BiotPorosityType: + default_porosity_tec: str = field( + default="0", + metadata={ + "name": "defaultPorosityTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_reference_porosity: Optional[str] = field( + default=None, + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + grain_bulk_modulus: Optional[str] = field( + default=None, + metadata={ + "name": "grainBulkModulus", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BlackOilFluidType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: Optional[str] = field( + default=None, + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hydrocarbon_formation_vol_factor_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonFormationVolFactorTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + hydrocarbon_viscosity_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonViscosityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + surface_densities: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceDensities", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + table_files: str = field( + default="{}", + metadata={ + "name": "tableFiles", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + water_compressibility: str = field( + default="0", + metadata={ + "name": "waterCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_formation_volume_factor: str = field( + default="0", + metadata={ + "name": "waterFormationVolumeFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_reference_pressure: str = field( + default="0", + metadata={ + "name": "waterReferencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_viscosity: str = field( + default="0", + metadata={ + "name": "waterViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BlueprintType: + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_full_quadrature_data: str = field( + default="0", + metadata={ + "name": "outputFullQuadratureData", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BoxType: + strike: str = field( + default="-90", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + x_max: Optional[str] = field( + default=None, + metadata={ + "name": "xMax", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_min: Optional[str] = field( + default=None, + metadata={ + "name": "xMin", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BrooksCoreyBakerRelativePermeabilityType: + gas_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "gasOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + water_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "waterOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BrooksCoreyCapillaryPressureType: + cap_pressure_epsilon: str = field( + default="1e-06", + metadata={ + "name": "capPressureEpsilon", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_cap_pressure_exponent_inv: str = field( + default="{2}", + metadata={ + "name": "phaseCapPressureExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_entry_pressure: str = field( + default="{1}", + metadata={ + "name": "phaseEntryPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BrooksCoreyRelativePermeabilityType: + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "phaseRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "phaseRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class BrooksCoreyStone2RelativePermeabilityType: + gas_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "gasOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + water_oil_rel_perm_exponent: str = field( + default="{1}", + metadata={ + "name": "waterOilRelPermExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class Co2BrineEzrokhiFluidType: + class Meta: + name = "CO2BrineEzrokhiFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: Optional[str] = field( + default=None, + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class Co2BrineEzrokhiThermalFluidType: + class Meta: + name = "CO2BrineEzrokhiThermalFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: Optional[str] = field( + default=None, + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class Co2BrinePhillipsFluidType: + class Meta: + name = "CO2BrinePhillipsFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: Optional[str] = field( + default=None, + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class Co2BrinePhillipsThermalFluidType: + class Meta: + name = "CO2BrinePhillipsThermalFluidType" + + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + flash_model_para_file: Optional[str] = field( + default=None, + metadata={ + "name": "flashModelParaFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: Optional[str] = field( + default=None, + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CarmanKozenyPermeabilityType: + anisotropy: str = field( + default="{1,1,1}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + particle_diameter: Optional[str] = field( + default=None, + metadata={ + "name": "particleDiameter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + sphericity: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CellElementRegionType: + cell_blocks: Optional[str] = field( + default=None, + metadata={ + "name": "cellBlocks", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + coarsening_ratio: str = field( + default="0", + metadata={ + "name": "coarseningRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + material_list: Optional[str] = field( + default=None, + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CeramicDamageType: + compressive_strength: Optional[str] = field( + default=None, + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + crack_speed: Optional[str] = field( + default=None, + metadata={ + "name": "crackSpeed", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + maximum_strength: Optional[str] = field( + default=None, + metadata={ + "name": "maximumStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + tensile_strength: Optional[str] = field( + default=None, + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ChomboIotype: + class Meta: + name = "ChomboIOType" + + begin_cycle: Optional[str] = field( + default=None, + metadata={ + "name": "beginCycle", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + input_path: str = field( + default="/INVALID_INPUT_PATH", + metadata={ + "name": "inputPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_path: Optional[str] = field( + default=None, + metadata={ + "name": "outputPath", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_chombo_pressures: str = field( + default="0", + metadata={ + "name": "useChomboPressures", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + wait_for_input: Optional[str] = field( + default=None, + metadata={ + "name": "waitForInput", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositeFunctionType: + expression: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + function_names: str = field( + default="{}", + metadata={ + "name": "functionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + variable_names: str = field( + default="{}", + metadata={ + "name": "variableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseFluidType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: Optional[str] = field( + default=None, + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: Optional[str] = field( + default=None, + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_critical_temperature: Optional[str] = field( + default=None, + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: Optional[str] = field( + default=None, + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: Optional[str] = field( + default=None, + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + equations_of_state: Optional[str] = field( + default=None, + metadata={ + "name": "equationsOfState", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseReservoirPoromechanicsInitializationType: + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: Optional[str] = field( + default=None, + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseStatisticsType: + compute_cflnumbers: str = field( + default="0", + metadata={ + "name": "computeCFLNumbers", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + compute_region_statistics: str = field( + default="1", + metadata={ + "name": "computeRegionStatistics", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + relperm_threshold: str = field( + default="1e-06", + metadata={ + "name": "relpermThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositonalTwoPhaseFluidPengRobinsonType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: Optional[str] = field( + default=None, + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: Optional[str] = field( + default=None, + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_critical_temperature: Optional[str] = field( + default=None, + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_critical_volume: str = field( + default="{0}", + metadata={ + "name": "componentCriticalVolume", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: Optional[str] = field( + default=None, + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: Optional[str] = field( + default=None, + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositonalTwoPhaseFluidSoaveRedlichKwongType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_acentric_factor: Optional[str] = field( + default=None, + metadata={ + "name": "componentAcentricFactor", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_binary_coeff: str = field( + default="{{0}}", + metadata={ + "name": "componentBinaryCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + component_critical_pressure: Optional[str] = field( + default=None, + metadata={ + "name": "componentCriticalPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_critical_temperature: Optional[str] = field( + default=None, + metadata={ + "name": "componentCriticalTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_critical_volume: str = field( + default="{0}", + metadata={ + "name": "componentCriticalVolume", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_molar_weight: Optional[str] = field( + default=None, + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: Optional[str] = field( + default=None, + metadata={ + "name": "componentNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + component_volume_shift: str = field( + default="{0}", + metadata={ + "name": "componentVolumeShift", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSinglePhaseFluidType: + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_viscosity: Optional[str] = field( + default=None, + metadata={ + "name": "defaultViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + density_model_type: str = field( + default="linear", + metadata={ + "name": "densityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="0", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosity_model_type: str = field( + default="linear", + metadata={ + "name": "viscosityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSolidCarmanKozenyPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSolidConstantPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSolidExponentialDecayPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSolidParallelPlatesPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSolidSlipDependentPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompressibleSolidWillisRichardsPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ConstantDiffusionType: + default_phase_diffusivity_multipliers: str = field( + default="{1}", + metadata={ + "name": "defaultPhaseDiffusivityMultipliers", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + diffusivity_components: Optional[str] = field( + default=None, + metadata={ + "name": "diffusivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ConstantPermeabilityType: + permeability_components: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CoulombType: + aperture_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "apertureTableName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + aperture_tolerance: str = field( + default="1e-09", + metadata={ + "name": "apertureTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cohesion: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + displacement_jump_threshold: str = field( + default="2.22045e-16", + metadata={ + "name": "displacementJumpThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + friction_coefficient: Optional[str] = field( + default=None, + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + penalty_stiffness: str = field( + default="0", + metadata={ + "name": "penaltyStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_stiffness: str = field( + default="0", + metadata={ + "name": "shearStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CustomPolarObjectType: + center: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + coefficients: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + length_vector: Optional[str] = field( + default=None, + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + normal: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: Optional[str] = field( + default=None, + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CylinderType: + first_face_center: Optional[str] = field( + default=None, + metadata={ + "name": "firstFaceCenter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + inner_radius: str = field( + default="-1", + metadata={ + "name": "innerRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + outer_radius: Optional[str] = field( + default=None, + metadata={ + "name": "outerRadius", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + second_face_center: Optional[str] = field( + default=None, + metadata={ + "name": "secondFaceCenter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DamageElasticIsotropicType: + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: Optional[str] = field( + default=None, + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_strain_energy: Optional[str] = field( + default=None, + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: Optional[str] = field( + default=None, + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DamageSpectralElasticIsotropicType: + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: Optional[str] = field( + default=None, + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_strain_energy: Optional[str] = field( + default=None, + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: Optional[str] = field( + default=None, + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DamageVolDevElasticIsotropicType: + compressive_strength: str = field( + default="0", + metadata={ + "name": "compressiveStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_fracture_energy: Optional[str] = field( + default=None, + metadata={ + "name": "criticalFractureEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_strain_energy: Optional[str] = field( + default=None, + metadata={ + "name": "criticalStrainEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + degradation_lower_limit: str = field( + default="0", + metadata={ + "name": "degradationLowerLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + delta_coefficient: str = field( + default="-1", + metadata={ + "name": "deltaCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ext_driving_force_flag: str = field( + default="0", + metadata={ + "name": "extDrivingForceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + length_scale: Optional[str] = field( + default=None, + metadata={ + "name": "lengthScale", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + tensile_strength: str = field( + default="0", + metadata={ + "name": "tensileStrength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DeadOilFluidType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: Optional[str] = field( + default=None, + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hydrocarbon_formation_vol_factor_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonFormationVolFactorTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + hydrocarbon_viscosity_table_names: str = field( + default="{}", + metadata={ + "name": "hydrocarbonViscosityTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + surface_densities: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceDensities", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + table_files: str = field( + default="{}", + metadata={ + "name": "tableFiles", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + water_compressibility: str = field( + default="0", + metadata={ + "name": "waterCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_formation_volume_factor: str = field( + default="0", + metadata={ + "name": "waterFormationVolumeFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_reference_pressure: str = field( + default="0", + metadata={ + "name": "waterReferencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + water_viscosity: str = field( + default="0", + metadata={ + "name": "waterViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DelftEggType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shape_parameter: str = field( + default="1", + metadata={ + "name": "defaultShapeParameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DirichletType: + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: Optional[str] = field( + default=None, + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DiscType: + center: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + length_vector: Optional[str] = field( + default=None, + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + normal: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + radius: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: Optional[str] = field( + default=None, + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class DruckerPragerType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_dilation_angle: str = field( + default="30", + metadata={ + "name": "defaultDilationAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening_rate: str = field( + default="0", + metadata={ + "name": "defaultHardeningRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ElasticIsotropicPressureDependentType: + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ElasticIsotropicType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ElasticOrthotropicType: + default_c11: str = field( + default="-1", + metadata={ + "name": "defaultC11", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c12: str = field( + default="-1", + metadata={ + "name": "defaultC12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c13: str = field( + default="-1", + metadata={ + "name": "defaultC13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c22: str = field( + default="-1", + metadata={ + "name": "defaultC22", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c23: str = field( + default="-1", + metadata={ + "name": "defaultC23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c33: str = field( + default="-1", + metadata={ + "name": "defaultC33", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c44: str = field( + default="-1", + metadata={ + "name": "defaultC44", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c55: str = field( + default="-1", + metadata={ + "name": "defaultC55", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c66: str = field( + default="-1", + metadata={ + "name": "defaultC66", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e1: str = field( + default="-1", + metadata={ + "name": "defaultE1", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e2: str = field( + default="-1", + metadata={ + "name": "defaultE2", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_e3: str = field( + default="-1", + metadata={ + "name": "defaultE3", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g12: str = field( + default="-1", + metadata={ + "name": "defaultG12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g13: str = field( + default="-1", + metadata={ + "name": "defaultG13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_g23: str = field( + default="-1", + metadata={ + "name": "defaultG23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu12: str = field( + default="-1", + metadata={ + "name": "defaultNu12", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu13: str = field( + default="-1", + metadata={ + "name": "defaultNu13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_nu23: str = field( + default="-1", + metadata={ + "name": "defaultNu23", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ElasticTransverseIsotropicType: + default_c11: str = field( + default="-1", + metadata={ + "name": "defaultC11", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c13: str = field( + default="-1", + metadata={ + "name": "defaultC13", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c33: str = field( + default="-1", + metadata={ + "name": "defaultC33", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c44: str = field( + default="-1", + metadata={ + "name": "defaultC44", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_c66: str = field( + default="-1", + metadata={ + "name": "defaultC66", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio_axial_transverse: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatioAxialTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio_transverse: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatioTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus_axial_transverse: str = field( + default="-1", + metadata={ + "name": "defaultShearModulusAxialTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus_axial: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulusAxial", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus_transverse: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulusTransverse", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ExponentialDecayPermeabilityType: + empirical_constant: Optional[str] = field( + default=None, + metadata={ + "name": "empiricalConstant", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_permeability: Optional[str] = field( + default=None, + metadata={ + "name": "initialPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ExtendedDruckerPragerType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_dilation_ratio: str = field( + default="1", + metadata={ + "name": "defaultDilationRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening: str = field( + default="0", + metadata={ + "name": "defaultHardening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_initial_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultInitialFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_residual_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultResidualFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class FieldSpecificationType: + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: Optional[str] = field( + default=None, + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class FileType: + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + + +@dataclass +class FiniteElementSpaceType: + formulation: str = field( + default="default", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|SEM", + }, + ) + order: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_virtual_elements: str = field( + default="0", + metadata={ + "name": "useVirtualElements", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class FrictionlessContactType: + aperture_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "apertureTableName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + aperture_tolerance: str = field( + default="1e-09", + metadata={ + "name": "apertureTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + displacement_jump_threshold: str = field( + default="2.22045e-16", + metadata={ + "name": "displacementJumpThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + penalty_stiffness: str = field( + default="0", + metadata={ + "name": "penaltyStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_stiffness: str = field( + default="0", + metadata={ + "name": "shearStiffness", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class HybridMimeticDiscretizationType: + inner_product_type: Optional[str] = field( + default=None, + metadata={ + "name": "innerProductType", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class HydrostaticEquilibriumType: + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component_fraction_vs_elevation_table_names: str = field( + default="{}", + metadata={ + "name": "componentFractionVsElevationTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + datum_elevation: Optional[str] = field( + default=None, + metadata={ + "name": "datumElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + datum_pressure: Optional[str] = field( + default=None, + metadata={ + "name": "datumPressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + elevation_increment_in_hydrostatic_pressure_table: str = field( + default="0.6096", + metadata={ + "name": "elevationIncrementInHydrostaticPressureTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + equilibration_tolerance: str = field( + default="0.001", + metadata={ + "name": "equilibrationTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_phase_name: Optional[str] = field( + default=None, + metadata={ + "name": "initialPhaseName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_number_of_equilibration_iterations: str = field( + default="5", + metadata={ + "name": "maxNumberOfEquilibrationIterations", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature_vs_elevation_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "temperatureVsElevationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class JfunctionCapillaryPressureType: + class Meta: + name = "JFunctionCapillaryPressureType" + + non_wetting_intermediate_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "nonWettingIntermediateJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + non_wetting_intermediate_surface_tension: str = field( + default="0", + metadata={ + "name": "nonWettingIntermediateSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + permeability_direction: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityDirection", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|XY|X|Y|Z", + }, + ) + permeability_exponent: str = field( + default="0.5", + metadata={ + "name": "permeabilityExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + porosity_exponent: str = field( + default="0.5", + metadata={ + "name": "porosityExponent", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + wetting_intermediate_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingIntermediateJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_intermediate_surface_tension: str = field( + default="0", + metadata={ + "name": "wettingIntermediateSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + wetting_non_wetting_jfunction_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingNonWettingJFunctionTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_non_wetting_surface_tension: str = field( + default="0", + metadata={ + "name": "wettingNonWettingSurfaceTension", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class LinearIsotropicDispersionType: + longitudinal_dispersivity: Optional[str] = field( + default=None, + metadata={ + "name": "longitudinalDispersivity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class LinearSolverParametersType: + amg_aggressive_coarsening_levels: str = field( + default="0", + metadata={ + "name": "amgAggressiveCoarseningLevels", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_aggressive_coarsening_paths: str = field( + default="1", + metadata={ + "name": "amgAggressiveCoarseningPaths", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_aggressive_interp_type: str = field( + default="multipass", + metadata={ + "name": "amgAggressiveInterpType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|extendedIStage2|standardStage2|extendedStage2|multipass|modifiedExtended|modifiedExtendedI|modifiedExtendedE|modifiedMultipass", + }, + ) + amg_coarse_solver: str = field( + default="direct", + metadata={ + "name": "amgCoarseSolver", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|jacobi|l1jacobi|fgs|sgs|l1sgs|chebyshev|direct|bgs", + }, + ) + amg_coarsening_type: str = field( + default="HMIS", + metadata={ + "name": "amgCoarseningType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|CLJP|RugeStueben|Falgout|PMIS|HMIS", + }, + ) + amg_interpolation_max_non_zeros: str = field( + default="4", + metadata={ + "name": "amgInterpolationMaxNonZeros", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_interpolation_type: str = field( + default="extendedI", + metadata={ + "name": "amgInterpolationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|modifiedClassical|direct|multipass|extendedI|standard|extended|directBAMG|modifiedExtended|modifiedExtendedI|modifiedExtendedE", + }, + ) + amg_null_space_type: str = field( + default="constantModes", + metadata={ + "name": "amgNullSpaceType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|constantModes|rigidBodyModes", + }, + ) + amg_num_functions: str = field( + default="1", + metadata={ + "name": "amgNumFunctions", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_num_sweeps: str = field( + default="1", + metadata={ + "name": "amgNumSweeps", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_relax_weight: str = field( + default="1", + metadata={ + "name": "amgRelaxWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + amg_separate_components: str = field( + default="0", + metadata={ + "name": "amgSeparateComponents", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + amg_smoother_type: str = field( + default="l1sgs", + metadata={ + "name": "amgSmootherType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|default|jacobi|l1jacobi|fgs|bgs|sgs|l1sgs|chebyshev|ilu0|ilut|ic0|ict", + }, + ) + amg_threshold: str = field( + default="0", + metadata={ + "name": "amgThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direct_check_residual: str = field( + default="0", + metadata={ + "name": "directCheckResidual", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_col_perm: str = field( + default="metis", + metadata={ + "name": "directColPerm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|MMD_AtplusA|MMD_AtA|colAMD|metis|parmetis", + }, + ) + direct_equil: str = field( + default="1", + metadata={ + "name": "directEquil", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_iter_ref: str = field( + default="1", + metadata={ + "name": "directIterRef", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_parallel: str = field( + default="1", + metadata={ + "name": "directParallel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_repl_tiny_pivot: str = field( + default="1", + metadata={ + "name": "directReplTinyPivot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direct_row_perm: str = field( + default="mc64", + metadata={ + "name": "directRowPerm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|mc64", + }, + ) + ilu_fill: str = field( + default="0", + metadata={ + "name": "iluFill", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + ilu_threshold: str = field( + default="0", + metadata={ + "name": "iluThreshold", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + krylov_adaptive_tol: str = field( + default="0", + metadata={ + "name": "krylovAdaptiveTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_max_iter: str = field( + default="200", + metadata={ + "name": "krylovMaxIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_max_restart: str = field( + default="200", + metadata={ + "name": "krylovMaxRestart", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + krylov_tol: str = field( + default="1e-06", + metadata={ + "name": "krylovTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + krylov_weakest_tol: str = field( + default="0.001", + metadata={ + "name": "krylovWeakestTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + preconditioner_type: str = field( + default="iluk", + metadata={ + "name": "preconditionerType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|none|jacobi|l1jacobi|fgs|sgs|l1sgs|chebyshev|iluk|ilut|icc|ict|amg|mgr|block|direct|bgs", + }, + ) + solver_type: str = field( + default="direct", + metadata={ + "name": "solverType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|direct|cg|gmres|fgmres|bicgstab|preconditioner", + }, + ) + stop_if_error: str = field( + default="1", + metadata={ + "name": "stopIfError", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + + +@dataclass +class ModifiedCamClayType: + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class MultiPhaseConstantThermalConductivityType: + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + thermal_conductivity_components: Optional[str] = field( + default=None, + metadata={ + "name": "thermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class MultiPhaseVolumeWeightedThermalConductivityType: + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_thermal_conductivity: Optional[str] = field( + default=None, + metadata={ + "name": "phaseThermalConductivity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + rock_thermal_conductivity_components: Optional[str] = field( + default=None, + metadata={ + "name": "rockThermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class MultiphasePoromechanicsInitializationType: + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: Optional[str] = field( + default=None, + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class MultivariableTableFunctionType: + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class NonlinearSolverParametersType: + allow_non_converged: str = field( + default="0", + metadata={ + "name": "allowNonConverged", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + coupling_type: str = field( + default="FullyImplicit", + metadata={ + "name": "couplingType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|FullyImplicit|Sequential", + }, + ) + line_search_action: str = field( + default="Attempt", + metadata={ + "name": "lineSearchAction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Attempt|Require", + }, + ) + line_search_cut_factor: str = field( + default="0.5", + metadata={ + "name": "lineSearchCutFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + line_search_interpolation_type: str = field( + default="Linear", + metadata={ + "name": "lineSearchInterpolationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Linear|Parabolic", + }, + ) + line_search_max_cuts: str = field( + default="4", + metadata={ + "name": "lineSearchMaxCuts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_allowed_residual_norm: str = field( + default="1e+09", + metadata={ + "name": "maxAllowedResidualNorm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_configuration_attempts: str = field( + default="10", + metadata={ + "name": "maxNumConfigurationAttempts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_sub_steps: str = field( + default="10", + metadata={ + "name": "maxSubSteps", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_time_step_cuts: str = field( + default="2", + metadata={ + "name": "maxTimeStepCuts", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + min_normalizer: str = field( + default="1e-12", + metadata={ + "name": "minNormalizer", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newton_max_iter: str = field( + default="5", + metadata={ + "name": "newtonMaxIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newton_min_iter: str = field( + default="1", + metadata={ + "name": "newtonMinIter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newton_tol: str = field( + default="1e-06", + metadata={ + "name": "newtonTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + nonlinear_acceleration_type: str = field( + default="None", + metadata={ + "name": "nonlinearAccelerationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Aitken", + }, + ) + sequential_convergence_criterion: str = field( + default="ResidualNorm", + metadata={ + "name": "sequentialConvergenceCriterion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|ResidualNorm|NumberOfNonlinearIterations", + }, + ) + subcycling: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + time_step_cut_factor: str = field( + default="0.5", + metadata={ + "name": "timeStepCutFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_decrease_factor: str = field( + default="0.5", + metadata={ + "name": "timeStepDecreaseFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_decrease_iter_limit: str = field( + default="0.7", + metadata={ + "name": "timeStepDecreaseIterLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_increase_factor: str = field( + default="2", + metadata={ + "name": "timeStepIncreaseFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_step_increase_iter_limit: str = field( + default="0.4", + metadata={ + "name": "timeStepIncreaseIterLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + norm_type: str = field( + default="Linfinity", + metadata={ + "name": "normType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Linfinity|L2", + }, + ) + + +@dataclass +class NullModelType: + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class Pmltype: + class Meta: + name = "PMLType" + + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + reflectivity: real32 = field( + default="0.001", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: Optional[str] = field( + default=None, + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + thickness_max_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "thicknessMaxXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + thickness_min_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "thicknessMinXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + wave_speed_max_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "waveSpeedMaxXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + wave_speed_min_xyz: str = field( + default="{-1,-1,-1}", + metadata={ + "name": "waveSpeedMinXYZ", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_max: str = field( + default="{3.40282e+38,3.40282e+38,3.40282e+38}", + metadata={ + "name": "xMax", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + x_min: str = field( + default="{-3.40282e+38,-3.40282e+38,-3.40282e+38}", + metadata={ + "name": "xMin", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PvtdriverType: + class Meta: + name = "PVTDriverType" + + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + feed_composition: Optional[str] = field( + default=None, + metadata={ + "name": "feedComposition", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + fluid: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + output_compressibility: str = field( + default="0", + metadata={ + "name": "outputCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_phase_composition: str = field( + default="0", + metadata={ + "name": "outputPhaseComposition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + pressure_control: Optional[str] = field( + default=None, + metadata={ + "name": "pressureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + steps: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + temperature_control: Optional[str] = field( + default=None, + metadata={ + "name": "temperatureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PackCollectionType: + disable_coord_collection: str = field( + default="0", + metadata={ + "name": "disableCoordCollection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + only_on_set_change: str = field( + default="0", + metadata={ + "name": "onlyOnSetChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + set_names: str = field( + default="{}", + metadata={ + "name": "setNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ParallelPlatesPermeabilityType: + transversal_permeability: str = field( + default="-1", + metadata={ + "name": "transversalPermeability", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ParameterType: + value: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ParticleFluidType: + collision_alpha: str = field( + default="1.27", + metadata={ + "name": "collisionAlpha", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + collision_beta: str = field( + default="1.5", + metadata={ + "name": "collisionBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + fluid_viscosity: str = field( + default="0.001", + metadata={ + "name": "fluidViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + hindered_settling_coefficient: str = field( + default="5.9", + metadata={ + "name": "hinderedSettlingCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_collisional_slip: str = field( + default="0", + metadata={ + "name": "isCollisionalSlip", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + particle_settling_model: Optional[str] = field( + default=None, + metadata={ + "name": "particleSettlingModel", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|Stokes|Intermediate|Turbulence", + }, + ) + proppant_density: str = field( + default="1400", + metadata={ + "name": "proppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: str = field( + default="0.0002", + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + slip_concentration: str = field( + default="0.1", + metadata={ + "name": "slipConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + sphericity: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ParticleMeshType: + header_file: Optional[str] = field( + default=None, + metadata={ + "name": "headerFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + particle_block_names: Optional[str] = field( + default=None, + metadata={ + "name": "particleBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + particle_file: Optional[str] = field( + default=None, + metadata={ + "name": "particleFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + particle_types: Optional[str] = field( + default=None, + metadata={ + "name": "particleTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ParticleRegionType: + material_list: Optional[str] = field( + default=None, + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + particle_blocks: str = field( + default="{}", + metadata={ + "name": "particleBlocks", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PerfectlyPlasticType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_yield_stress: str = field( + default="1.79769e+308", + metadata={ + "name": "defaultYieldStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PerforationType: + distance_from_head: Optional[str] = field( + default=None, + metadata={ + "name": "distanceFromHead", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + skin_factor: str = field( + default="0", + metadata={ + "name": "skinFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + transmissibility: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PermeabilityBaseType: + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousDelftEggType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousDruckerPragerType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousElasticIsotropicType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousElasticOrthotropicType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousElasticTransverseIsotropicType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousExtendedDruckerPragerType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PorousModifiedCamClayType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PressurePorosityType: + compressibility: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_reference_porosity: Optional[str] = field( + default=None, + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: Optional[str] = field( + default=None, + metadata={ + "name": "referencePressure", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ProppantPermeabilityType: + max_proppant_concentration: Optional[str] = field( + default=None, + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: Optional[str] = field( + default=None, + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ProppantPorosityType: + default_reference_porosity: Optional[str] = field( + default=None, + metadata={ + "name": "defaultReferencePorosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_proppant_concentration: Optional[str] = field( + default=None, + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ProppantSlurryFluidType: + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_component_density: str = field( + default="{0}", + metadata={ + "name": "defaultComponentDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + default_component_viscosity: str = field( + default="{0}", + metadata={ + "name": "defaultComponentViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + default_compressibility: str = field( + default="{0}", + metadata={ + "name": "defaultCompressibility", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + flow_behavior_index: str = field( + default="{0}", + metadata={ + "name": "flowBehaviorIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + flow_consistency_index: str = field( + default="{0}", + metadata={ + "name": "flowConsistencyIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="100000", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_proppant_density: str = field( + default="1400", + metadata={ + "name": "referenceProppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ProppantSolidProppantPermeabilityType: + permeability_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "permeabilityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + porosity_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "porosityModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_internal_energy_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidInternalEnergyModelName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_model_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidModelName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PythonType: + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ReactiveBrineThermalType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: Optional[str] = field( + default=None, + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ReactiveBrineType: + check_pvttables_ranges: str = field( + default="1", + metadata={ + "name": "checkPVTTablesRanges", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + component_molar_weight: str = field( + default="{0}", + metadata={ + "name": "componentMolarWeight", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_pvtpara_files: Optional[str] = field( + default=None, + metadata={ + "name": "phasePVTParaFiles", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ReactiveFluidDriverType: + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + feed_composition: Optional[str] = field( + default=None, + metadata={ + "name": "feedComposition", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + fluid: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + pressure_control: Optional[str] = field( + default=None, + metadata={ + "name": "pressureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + steps: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + temperature_control: Optional[str] = field( + default=None, + metadata={ + "name": "temperatureControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class RectangleType: + dimensions: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + length_vector: Optional[str] = field( + default=None, + metadata={ + "name": "lengthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + normal: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + origin: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + tolerance: str = field( + default="1e-05", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + width_vector: Optional[str] = field( + default=None, + metadata={ + "name": "widthVector", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class RelpermDriverType: + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + relperm: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + steps: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class RestartType: + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class RunType: + args: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + auto_partition: Optional[str] = field( + default=None, + metadata={ + "name": "autoPartition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + mesh_sizes: str = field( + default="{0}", + metadata={ + "name": "meshSizes", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + nodes: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + scale_list: str = field( + default="{0}", + metadata={ + "name": "scaleList", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + scaling: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + tasks_per_node: Optional[str] = field( + default=None, + metadata={ + "name": "tasksPerNode", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + threads_per_task: str = field( + default="0", + metadata={ + "name": "threadsPerTask", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + time_limit: str = field( + default="0", + metadata={ + "name": "timeLimit", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + + +@dataclass +class SiloType: + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + field_names: str = field( + default="{}", + metadata={ + "name": "fieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + only_plot_specified_field_names: str = field( + default="0", + metadata={ + "name": "onlyPlotSpecifiedFieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_file_root: str = field( + default="plot", + metadata={ + "name": "plotFileRoot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_cell_element_mesh: str = field( + default="1", + metadata={ + "name": "writeCellElementMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_edge_mesh: str = field( + default="0", + metadata={ + "name": "writeEdgeMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_femfaces: str = field( + default="0", + metadata={ + "name": "writeFEMFaces", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_face_element_mesh: str = field( + default="1", + metadata={ + "name": "writeFaceElementMesh", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseConstantThermalConductivityType: + thermal_conductivity_components: Optional[str] = field( + default=None, + metadata={ + "name": "thermalConductivityComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhasePoromechanicsInitializationType: + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: Optional[str] = field( + default=None, + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseReservoirPoromechanicsInitializationType: + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + perform_stress_initialization: Optional[str] = field( + default=None, + metadata={ + "name": "performStressInitialization", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseStatisticsType: + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SlipDependentPermeabilityType: + initial_permeability: Optional[str] = field( + default=None, + metadata={ + "name": "initialPermeability", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + max_perm_multiplier: Optional[str] = field( + default=None, + metadata={ + "name": "maxPermMultiplier", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + shear_disp_threshold: Optional[str] = field( + default=None, + metadata={ + "name": "shearDispThreshold", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidInternalEnergyType: + reference_internal_energy: Optional[str] = field( + default=None, + metadata={ + "name": "referenceInternalEnergy", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_temperature: Optional[str] = field( + default=None, + metadata={ + "name": "referenceTemperature", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + volumetric_heat_capacity: Optional[str] = field( + default=None, + metadata={ + "name": "volumetricHeatCapacity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidMechanicsStateResetType: + disable_inelasticity: str = field( + default="0", + metadata={ + "name": "disableInelasticity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reset_displacements: str = field( + default="1", + metadata={ + "name": "resetDisplacements", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidMechanicsStatisticsType: + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SoloEventType: + halt_event: list["HaltEventType"] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: list["PeriodicEventType"] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: list["SoloEventType"] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_cycle: str = field( + default="-1", + metadata={ + "name": "targetCycle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_timestep: str = field( + default="1", + metadata={ + "name": "targetExactTimestep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_time: str = field( + default="-1", + metadata={ + "name": "targetTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SourceFluxType: + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component: str = field( + default="-1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: Optional[str] = field( + default=None, + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SurfaceElementRegionType: + default_aperture: Optional[str] = field( + default=None, + metadata={ + "name": "defaultAperture", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + face_block: str = field( + default="FractureSubRegion", + metadata={ + "name": "faceBlock", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + material_list: Optional[str] = field( + default=None, + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + sub_region_type: str = field( + default="faceElement", + metadata={ + "name": "subRegionType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|faceElement|embeddedElement", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SymbolicFunctionType: + expression: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + variable_names: Optional[str] = field( + default=None, + metadata={ + "name": "variableNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TableCapillaryPressureType: + non_wetting_intermediate_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "nonWettingIntermediateCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + wetting_intermediate_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingIntermediateCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + wetting_non_wetting_cap_pressure_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "wettingNonWettingCapPressureTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TableFunctionType: + coordinate_files: str = field( + default="{}", + metadata={ + "name": "coordinateFiles", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^*?<>\|:\";,\s]+\s*,\s*)*[^*?<>\|:\";,\s]+\s*)?\}\s*", + }, + ) + coordinates: str = field( + default="{0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + input_var_names: str = field( + default="{}", + metadata={ + "name": "inputVarNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + interpolation: str = field( + default="linear", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|linear|nearest|upper|lower", + }, + ) + values: str = field( + default="{0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + voxel_file: Optional[str] = field( + default=None, + metadata={ + "name": "voxelFile", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TableRelativePermeabilityHysteresisType: + drainage_non_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageNonWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + drainage_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + drainage_wetting_non_wetting_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "drainageWettingNonWettingRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + imbibition_non_wetting_rel_perm_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "imbibitionNonWettingRelPermTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + imbibition_wetting_rel_perm_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "imbibitionWettingRelPermTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + jerauld_parameter_a: str = field( + default="0.1", + metadata={ + "name": "jerauldParameterA", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + jerauld_parameter_b: str = field( + default="0", + metadata={ + "name": "jerauldParameterB", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + killough_curvature_parameter: str = field( + default="1", + metadata={ + "name": "killoughCurvatureParameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + three_phase_interpolator: str = field( + default="BAKER", + metadata={ + "name": "threePhaseInterpolator", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|BAKER|STONEII", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TableRelativePermeabilityType: + non_wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "nonWettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + three_phase_interpolator: str = field( + default="BAKER", + metadata={ + "name": "threePhaseInterpolator", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|BAKER|STONEII", + }, + ) + wetting_intermediate_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "wettingIntermediateRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + wetting_non_wetting_rel_perm_table_names: str = field( + default="{}", + metadata={ + "name": "wettingNonWettingRelPermTableNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ThermalCompressibleSinglePhaseFluidType: + compressibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_viscosity: Optional[str] = field( + default=None, + metadata={ + "name": "defaultViscosity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + density_model_type: str = field( + default="linear", + metadata={ + "name": "densityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + internal_energy_model_type: str = field( + default="linear", + metadata={ + "name": "internalEnergyModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + reference_density: str = field( + default="1000", + metadata={ + "name": "referenceDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_internal_energy: str = field( + default="0.001", + metadata={ + "name": "referenceInternalEnergy", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_pressure: str = field( + default="0", + metadata={ + "name": "referencePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_temperature: str = field( + default="0", + metadata={ + "name": "referenceTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + reference_viscosity: str = field( + default="0.001", + metadata={ + "name": "referenceViscosity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + thermal_expansion_coeff: str = field( + default="0", + metadata={ + "name": "thermalExpansionCoeff", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosibility: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + viscosity_model_type: str = field( + default="linear", + metadata={ + "name": "viscosityModelType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|exponential|linear|quadratic", + }, + ) + volumetric_heat_capacity: str = field( + default="0", + metadata={ + "name": "volumetricHeatCapacity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ThickPlaneType: + normal: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + origin: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + thickness: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TimeHistoryType: + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + filename: str = field( + default="TimeHistory", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + format: str = field( + default="hdf", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + sources: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TractionType: + bc_application_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "bcApplicationTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + begin_time: str = field( + default="-1e+99", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + direction: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + end_time: str = field( + default="1e+99", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function_name: Optional[str] = field( + default=None, + metadata={ + "name": "functionName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_condition: str = field( + default="0", + metadata={ + "name": "initialCondition", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + input_stress: str = field( + default="{0,0,0,0,0,0}", + metadata={ + "name": "inputStress", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){5}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + object_path: Optional[str] = field( + default=None, + metadata={ + "name": "objectPath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + set_names: Optional[str] = field( + default=None, + metadata={ + "name": "setNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + traction_type: str = field( + default="vector", + metadata={ + "name": "tractionType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|vector|normal|stress", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TriaxialDriverType: + axial_control: Optional[str] = field( + default=None, + metadata={ + "name": "axialControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + baseline: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + initial_stress: Optional[str] = field( + default=None, + metadata={ + "name": "initialStress", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + material: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + mode: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|mixedControl|strainControl|stressControl", + }, + ) + output: str = field( + default="none", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + radial_control: Optional[str] = field( + default=None, + metadata={ + "name": "radialControl", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + steps: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TwoPointFluxApproximationType: + area_rel_tol: str = field( + default="1e-08", + metadata={ + "name": "areaRelTol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + mean_perm_coefficient: str = field( + default="1", + metadata={ + "name": "meanPermCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + upwinding_scheme: str = field( + default="PPU", + metadata={ + "name": "upwindingScheme", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|PPU|C1PPU", + }, + ) + use_pedfm: str = field( + default="0", + metadata={ + "name": "usePEDFM", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class Vtktype: + class Meta: + name = "VTKType" + + child_directory: Optional[str] = field( + default=None, + metadata={ + "name": "childDirectory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + field_names: str = field( + default="{}", + metadata={ + "name": "fieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + format: str = field( + default="binary", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|binary|ascii", + }, + ) + level_names: str = field( + default="{}", + metadata={ + "name": "levelNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + only_plot_specified_field_names: str = field( + default="0", + metadata={ + "name": "onlyPlotSpecifiedFieldNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_region_type: str = field( + default="all", + metadata={ + "name": "outputRegionType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|cell|well|surface|particle|all", + }, + ) + parallel_threads: str = field( + default="1", + metadata={ + "name": "parallelThreads", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + plot_file_root: str = field( + default="VTK", + metadata={ + "name": "plotFileRoot", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + plot_level: str = field( + default="1", + metadata={ + "name": "plotLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_femfaces: str = field( + default="0", + metadata={ + "name": "writeFEMFaces", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + write_ghost_cells: str = field( + default="0", + metadata={ + "name": "writeGhostCells", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class VanGenuchtenBakerRelativePermeabilityType: + gas_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "gasOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + water_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "waterOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class VanGenuchtenCapillaryPressureType: + cap_pressure_epsilon: str = field( + default="1e-06", + metadata={ + "name": "capPressureEpsilon", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + phase_cap_pressure_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "phaseCapPressureExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_cap_pressure_multiplier: str = field( + default="{1}", + metadata={ + "name": "phaseCapPressureMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class VanGenuchtenStone2RelativePermeabilityType: + gas_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "gasOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + gas_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "gasOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_min_volume_fraction: str = field( + default="{0}", + metadata={ + "name": "phaseMinVolumeFraction", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + phase_names: Optional[str] = field( + default=None, + metadata={ + "name": "phaseNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + water_oil_rel_perm_exponent_inv: str = field( + default="{0.5}", + metadata={ + "name": "waterOilRelPermExponentInv", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + water_oil_rel_perm_max_value: str = field( + default="{0}", + metadata={ + "name": "waterOilRelPermMaxValue", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ViscoDruckerPragerType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_dilation_angle: str = field( + default="30", + metadata={ + "name": "defaultDilationAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening_rate: str = field( + default="0", + metadata={ + "name": "defaultHardeningRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: Optional[str] = field( + default=None, + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ViscoExtendedDruckerPragerType: + default_bulk_modulus: str = field( + default="-1", + metadata={ + "name": "defaultBulkModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_cohesion: str = field( + default="0", + metadata={ + "name": "defaultCohesion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_dilation_ratio: str = field( + default="1", + metadata={ + "name": "defaultDilationRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_hardening: str = field( + default="0", + metadata={ + "name": "defaultHardening", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_initial_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultInitialFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_poisson_ratio: str = field( + default="-1", + metadata={ + "name": "defaultPoissonRatio", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_residual_friction_angle: str = field( + default="30", + metadata={ + "name": "defaultResidualFrictionAngle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_young_modulus: str = field( + default="-1", + metadata={ + "name": "defaultYoungModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: Optional[str] = field( + default=None, + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ViscoModifiedCamClayType: + default_csl_slope: str = field( + default="1", + metadata={ + "name": "defaultCslSlope", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_density: Optional[str] = field( + default=None, + metadata={ + "name": "defaultDensity", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_drained_linear_tec: str = field( + default="0", + metadata={ + "name": "defaultDrainedLinearTEC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_pre_consolidation_pressure: str = field( + default="-1.5", + metadata={ + "name": "defaultPreConsolidationPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_recompression_index: str = field( + default="0.002", + metadata={ + "name": "defaultRecompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_pressure: str = field( + default="-1", + metadata={ + "name": "defaultRefPressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_ref_strain_vol: str = field( + default="0", + metadata={ + "name": "defaultRefStrainVol", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_shear_modulus: str = field( + default="-1", + metadata={ + "name": "defaultShearModulus", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + default_virgin_compression_index: str = field( + default="0.005", + metadata={ + "name": "defaultVirginCompressionIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + relaxation_time: Optional[str] = field( + default=None, + metadata={ + "name": "relaxationTime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class WellControlsType: + control: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|BHP|phaseVolRate|totalVolRate|uninitialized", + }, + ) + enable_crossflow: str = field( + default="1", + metadata={ + "name": "enableCrossflow", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_pressure_coefficient: str = field( + default="0.1", + metadata={ + "name": "initialPressureCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + injection_stream: str = field( + default="{-1}", + metadata={ + "name": "injectionStream", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + injection_temperature: str = field( + default="-1", + metadata={ + "name": "injectionTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reference_elevation: Optional[str] = field( + default=None, + metadata={ + "name": "referenceElevation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + status_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "statusTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + surface_pressure: str = field( + default="0", + metadata={ + "name": "surfacePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + surface_temperature: str = field( + default="0", + metadata={ + "name": "surfaceTemperature", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_bhp: str = field( + default="0", + metadata={ + "name": "targetBHP", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_bhptable_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetBHPTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_phase_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetPhaseName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_phase_rate: str = field( + default="0", + metadata={ + "name": "targetPhaseRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_rate_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetPhaseRateTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_total_rate: str = field( + default="0", + metadata={ + "name": "targetTotalRate", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_total_rate_table_name: Optional[str] = field( + default=None, + metadata={ + "name": "targetTotalRateTableName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + type_value: Optional[str] = field( + default=None, + metadata={ + "name": "type", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|producer|injector", + }, + ) + use_surface_conditions: str = field( + default="0", + metadata={ + "name": "useSurfaceConditions", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class WellElementRegionType: + material_list: Optional[str] = field( + default=None, + metadata={ + "name": "materialList", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + mesh_body: Optional[str] = field( + default=None, + metadata={ + "name": "meshBody", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class WillisRichardsPermeabilityType: + dilation_coefficient: Optional[str] = field( + default=None, + metadata={ + "name": "dilationCoefficient", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_frac_aperture: Optional[str] = field( + default=None, + metadata={ + "name": "maxFracAperture", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + ref_closure_stress: Optional[str] = field( + default=None, + metadata={ + "name": "refClosureStress", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class AcousticFirstOrderSemtype: + class Meta: + name = "AcousticFirstOrderSEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_source_delay: real32 = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: real32 = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class AcousticSemtype: + class Meta: + name = "AcousticSEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class AcousticVtisemtype: + class Meta: + name = "AcousticVTISEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseFvmtype: + class Meta: + name = "CompositionalMultiphaseFVMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cont_multiplier_dbc: str = field( + default="0.5", + metadata={ + "name": "contMultiplierDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + continuation_dbc: str = field( + default="1", + metadata={ + "name": "continuationDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + kappamin_dbc: str = field( + default="1e-20", + metadata={ + "name": "kappaminDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="0.5", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_temperature_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativeTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_comp_dens: str = field( + default="1e-10", + metadata={ + "name": "minCompDens", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + miscible_dbc: str = field( + default="0", + metadata={ + "name": "miscibleDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + omega_dbc: str = field( + default="1", + metadata={ + "name": "omegaDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + scaling_type: str = field( + default="Global", + metadata={ + "name": "scalingType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|Global|Local", + }, + ) + solution_change_scaling_factor: str = field( + default="0.5", + metadata={ + "name": "solutionChangeScalingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_flow_cfl: str = field( + default="-1", + metadata={ + "name": "targetFlowCFL", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_vol_fraction_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetPhaseVolFractionChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + target_relative_pressure_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativePressureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_relative_temperature_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativeTemperatureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_dbc: str = field( + default="0", + metadata={ + "name": "useDBC", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_simple_accumulation: str = field( + default="0", + metadata={ + "name": "useSimpleAccumulation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_total_mass_equation: str = field( + default="1", + metadata={ + "name": "useTotalMassEquation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseHybridFvmtype: + class Meta: + name = "CompositionalMultiphaseHybridFVMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="0.5", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_temperature_change: str = field( + default="0.5", + metadata={ + "name": "maxRelativeTemperatureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_comp_dens: str = field( + default="1e-10", + metadata={ + "name": "minCompDens", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + solution_change_scaling_factor: str = field( + default="0.5", + metadata={ + "name": "solutionChangeScalingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_flow_cfl: str = field( + default="-1", + metadata={ + "name": "targetFlowCFL", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_phase_vol_fraction_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetPhaseVolFractionChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + target_relative_pressure_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativePressureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_relative_temperature_change_in_time_step: str = field( + default="0.2", + metadata={ + "name": "targetRelativeTemperatureChangeInTimeStep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + temperature: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_simple_accumulation: str = field( + default="0", + metadata={ + "name": "useSimpleAccumulation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_total_mass_equation: str = field( + default="1", + metadata={ + "name": "useTotalMassEquation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseReservoirPoromechanicsType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reservoir_and_wells_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "reservoirAndWellsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + stabilization_multiplier: str = field( + default="1", + metadata={ + "name": "stabilizationMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_region_names: str = field( + default="{}", + metadata={ + "name": "stabilizationRegionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + stabilization_type: str = field( + default="None", + metadata={ + "name": "stabilizationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Global|Local", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseReservoirType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + well_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class CompositionalMultiphaseWellType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + well_controls: list[WellControlsType] = field( + default_factory=list, + metadata={ + "name": "WellControls", + "type": "Element", + "namespace": "", + }, + ) + allow_local_comp_density_chopping: str = field( + default="1", + metadata={ + "name": "allowLocalCompDensityChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="1", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_relative_pressure_change: str = field( + default="1", + metadata={ + "name": "maxRelativePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + use_mass: str = field( + default="0", + metadata={ + "name": "useMass", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ConstitutiveType: + biot_porosity: list[BiotPorosityType] = field( + default_factory=list, + metadata={ + "name": "BiotPorosity", + "type": "Element", + "namespace": "", + }, + ) + black_oil_fluid: list[BlackOilFluidType] = field( + default_factory=list, + metadata={ + "name": "BlackOilFluid", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_baker_relative_permeability: list[ + BrooksCoreyBakerRelativePermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyBakerRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_capillary_pressure: list[BrooksCoreyCapillaryPressureType] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_relative_permeability: list[ + BrooksCoreyRelativePermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + brooks_corey_stone2_relative_permeability: list[ + BrooksCoreyStone2RelativePermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "BrooksCoreyStone2RelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_ezrokhi_fluid: list[Co2BrineEzrokhiFluidType] = field( + default_factory=list, + metadata={ + "name": "CO2BrineEzrokhiFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_ezrokhi_thermal_fluid: list[Co2BrineEzrokhiThermalFluidType] = field( + default_factory=list, + metadata={ + "name": "CO2BrineEzrokhiThermalFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_phillips_fluid: list[Co2BrinePhillipsFluidType] = field( + default_factory=list, + metadata={ + "name": "CO2BrinePhillipsFluid", + "type": "Element", + "namespace": "", + }, + ) + co2_brine_phillips_thermal_fluid: list[Co2BrinePhillipsThermalFluidType] = field( + default_factory=list, + metadata={ + "name": "CO2BrinePhillipsThermalFluid", + "type": "Element", + "namespace": "", + }, + ) + carman_kozeny_permeability: list[CarmanKozenyPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "CarmanKozenyPermeability", + "type": "Element", + "namespace": "", + }, + ) + ceramic_damage: list[CeramicDamageType] = field( + default_factory=list, + metadata={ + "name": "CeramicDamage", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_fluid: list[CompositionalMultiphaseFluidType] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseFluid", + "type": "Element", + "namespace": "", + }, + ) + compositonal_two_phase_fluid_peng_robinson: list[ + CompositonalTwoPhaseFluidPengRobinsonType + ] = field( + default_factory=list, + metadata={ + "name": "CompositonalTwoPhaseFluidPengRobinson", + "type": "Element", + "namespace": "", + }, + ) + compositonal_two_phase_fluid_soave_redlich_kwong: list[ + CompositonalTwoPhaseFluidSoaveRedlichKwongType + ] = field( + default_factory=list, + metadata={ + "name": "CompositonalTwoPhaseFluidSoaveRedlichKwong", + "type": "Element", + "namespace": "", + }, + ) + compressible_single_phase_fluid: list[CompressibleSinglePhaseFluidType] = field( + default_factory=list, + metadata={ + "name": "CompressibleSinglePhaseFluid", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_carman_kozeny_permeability: list[ + CompressibleSolidCarmanKozenyPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidCarmanKozenyPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_constant_permeability: list[ + CompressibleSolidConstantPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidConstantPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_exponential_decay_permeability: list[ + CompressibleSolidExponentialDecayPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidExponentialDecayPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_parallel_plates_permeability: list[ + CompressibleSolidParallelPlatesPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidParallelPlatesPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_slip_dependent_permeability: list[ + CompressibleSolidSlipDependentPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidSlipDependentPermeability", + "type": "Element", + "namespace": "", + }, + ) + compressible_solid_willis_richards_permeability: list[ + CompressibleSolidWillisRichardsPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "CompressibleSolidWillisRichardsPermeability", + "type": "Element", + "namespace": "", + }, + ) + constant_diffusion: list[ConstantDiffusionType] = field( + default_factory=list, + metadata={ + "name": "ConstantDiffusion", + "type": "Element", + "namespace": "", + }, + ) + constant_permeability: list[ConstantPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "ConstantPermeability", + "type": "Element", + "namespace": "", + }, + ) + coulomb: list[CoulombType] = field( + default_factory=list, + metadata={ + "name": "Coulomb", + "type": "Element", + "namespace": "", + }, + ) + damage_elastic_isotropic: list[DamageElasticIsotropicType] = field( + default_factory=list, + metadata={ + "name": "DamageElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + damage_spectral_elastic_isotropic: list[DamageSpectralElasticIsotropicType] = field( + default_factory=list, + metadata={ + "name": "DamageSpectralElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + damage_vol_dev_elastic_isotropic: list[DamageVolDevElasticIsotropicType] = field( + default_factory=list, + metadata={ + "name": "DamageVolDevElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + dead_oil_fluid: list[DeadOilFluidType] = field( + default_factory=list, + metadata={ + "name": "DeadOilFluid", + "type": "Element", + "namespace": "", + }, + ) + delft_egg: list[DelftEggType] = field( + default_factory=list, + metadata={ + "name": "DelftEgg", + "type": "Element", + "namespace": "", + }, + ) + drucker_prager: list[DruckerPragerType] = field( + default_factory=list, + metadata={ + "name": "DruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + elastic_isotropic: list[ElasticIsotropicType] = field( + default_factory=list, + metadata={ + "name": "ElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + elastic_isotropic_pressure_dependent: list[ + ElasticIsotropicPressureDependentType + ] = field( + default_factory=list, + metadata={ + "name": "ElasticIsotropicPressureDependent", + "type": "Element", + "namespace": "", + }, + ) + elastic_orthotropic: list[ElasticOrthotropicType] = field( + default_factory=list, + metadata={ + "name": "ElasticOrthotropic", + "type": "Element", + "namespace": "", + }, + ) + elastic_transverse_isotropic: list[ElasticTransverseIsotropicType] = field( + default_factory=list, + metadata={ + "name": "ElasticTransverseIsotropic", + "type": "Element", + "namespace": "", + }, + ) + exponential_decay_permeability: list[ExponentialDecayPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "ExponentialDecayPermeability", + "type": "Element", + "namespace": "", + }, + ) + extended_drucker_prager: list[ExtendedDruckerPragerType] = field( + default_factory=list, + metadata={ + "name": "ExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + frictionless_contact: list[FrictionlessContactType] = field( + default_factory=list, + metadata={ + "name": "FrictionlessContact", + "type": "Element", + "namespace": "", + }, + ) + jfunction_capillary_pressure: list[JfunctionCapillaryPressureType] = field( + default_factory=list, + metadata={ + "name": "JFunctionCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + linear_isotropic_dispersion: list[LinearIsotropicDispersionType] = field( + default_factory=list, + metadata={ + "name": "LinearIsotropicDispersion", + "type": "Element", + "namespace": "", + }, + ) + modified_cam_clay: list[ModifiedCamClayType] = field( + default_factory=list, + metadata={ + "name": "ModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + multi_phase_constant_thermal_conductivity: list[ + MultiPhaseConstantThermalConductivityType + ] = field( + default_factory=list, + metadata={ + "name": "MultiPhaseConstantThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + multi_phase_volume_weighted_thermal_conductivity: list[ + MultiPhaseVolumeWeightedThermalConductivityType + ] = field( + default_factory=list, + metadata={ + "name": "MultiPhaseVolumeWeightedThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + null_model: list[NullModelType] = field( + default_factory=list, + metadata={ + "name": "NullModel", + "type": "Element", + "namespace": "", + }, + ) + parallel_plates_permeability: list[ParallelPlatesPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "ParallelPlatesPermeability", + "type": "Element", + "namespace": "", + }, + ) + particle_fluid: list[ParticleFluidType] = field( + default_factory=list, + metadata={ + "name": "ParticleFluid", + "type": "Element", + "namespace": "", + }, + ) + perfectly_plastic: list[PerfectlyPlasticType] = field( + default_factory=list, + metadata={ + "name": "PerfectlyPlastic", + "type": "Element", + "namespace": "", + }, + ) + permeability_base: list[PermeabilityBaseType] = field( + default_factory=list, + metadata={ + "name": "PermeabilityBase", + "type": "Element", + "namespace": "", + }, + ) + porous_delft_egg: list[PorousDelftEggType] = field( + default_factory=list, + metadata={ + "name": "PorousDelftEgg", + "type": "Element", + "namespace": "", + }, + ) + porous_drucker_prager: list[PorousDruckerPragerType] = field( + default_factory=list, + metadata={ + "name": "PorousDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_isotropic: list[PorousElasticIsotropicType] = field( + default_factory=list, + metadata={ + "name": "PorousElasticIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_orthotropic: list[PorousElasticOrthotropicType] = field( + default_factory=list, + metadata={ + "name": "PorousElasticOrthotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_elastic_transverse_isotropic: list[ + PorousElasticTransverseIsotropicType + ] = field( + default_factory=list, + metadata={ + "name": "PorousElasticTransverseIsotropic", + "type": "Element", + "namespace": "", + }, + ) + porous_extended_drucker_prager: list[PorousExtendedDruckerPragerType] = field( + default_factory=list, + metadata={ + "name": "PorousExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + porous_modified_cam_clay: list[PorousModifiedCamClayType] = field( + default_factory=list, + metadata={ + "name": "PorousModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + pressure_porosity: list[PressurePorosityType] = field( + default_factory=list, + metadata={ + "name": "PressurePorosity", + "type": "Element", + "namespace": "", + }, + ) + proppant_permeability: list[ProppantPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "ProppantPermeability", + "type": "Element", + "namespace": "", + }, + ) + proppant_porosity: list[ProppantPorosityType] = field( + default_factory=list, + metadata={ + "name": "ProppantPorosity", + "type": "Element", + "namespace": "", + }, + ) + proppant_slurry_fluid: list[ProppantSlurryFluidType] = field( + default_factory=list, + metadata={ + "name": "ProppantSlurryFluid", + "type": "Element", + "namespace": "", + }, + ) + proppant_solid_proppant_permeability: list[ + ProppantSolidProppantPermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "ProppantSolidProppantPermeability", + "type": "Element", + "namespace": "", + }, + ) + reactive_brine: list[ReactiveBrineType] = field( + default_factory=list, + metadata={ + "name": "ReactiveBrine", + "type": "Element", + "namespace": "", + }, + ) + reactive_brine_thermal: list[ReactiveBrineThermalType] = field( + default_factory=list, + metadata={ + "name": "ReactiveBrineThermal", + "type": "Element", + "namespace": "", + }, + ) + single_phase_constant_thermal_conductivity: list[ + SinglePhaseConstantThermalConductivityType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseConstantThermalConductivity", + "type": "Element", + "namespace": "", + }, + ) + slip_dependent_permeability: list[SlipDependentPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "SlipDependentPermeability", + "type": "Element", + "namespace": "", + }, + ) + solid_internal_energy: list[SolidInternalEnergyType] = field( + default_factory=list, + metadata={ + "name": "SolidInternalEnergy", + "type": "Element", + "namespace": "", + }, + ) + table_capillary_pressure: list[TableCapillaryPressureType] = field( + default_factory=list, + metadata={ + "name": "TableCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + table_relative_permeability: list[TableRelativePermeabilityType] = field( + default_factory=list, + metadata={ + "name": "TableRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + table_relative_permeability_hysteresis: list[ + TableRelativePermeabilityHysteresisType + ] = field( + default_factory=list, + metadata={ + "name": "TableRelativePermeabilityHysteresis", + "type": "Element", + "namespace": "", + }, + ) + thermal_compressible_single_phase_fluid: list[ + ThermalCompressibleSinglePhaseFluidType + ] = field( + default_factory=list, + metadata={ + "name": "ThermalCompressibleSinglePhaseFluid", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_baker_relative_permeability: list[ + VanGenuchtenBakerRelativePermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenBakerRelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_capillary_pressure: list[VanGenuchtenCapillaryPressureType] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenCapillaryPressure", + "type": "Element", + "namespace": "", + }, + ) + van_genuchten_stone2_relative_permeability: list[ + VanGenuchtenStone2RelativePermeabilityType + ] = field( + default_factory=list, + metadata={ + "name": "VanGenuchtenStone2RelativePermeability", + "type": "Element", + "namespace": "", + }, + ) + visco_drucker_prager: list[ViscoDruckerPragerType] = field( + default_factory=list, + metadata={ + "name": "ViscoDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + visco_extended_drucker_prager: list[ViscoExtendedDruckerPragerType] = field( + default_factory=list, + metadata={ + "name": "ViscoExtendedDruckerPrager", + "type": "Element", + "namespace": "", + }, + ) + visco_modified_cam_clay: list[ViscoModifiedCamClayType] = field( + default_factory=list, + metadata={ + "name": "ViscoModifiedCamClay", + "type": "Element", + "namespace": "", + }, + ) + willis_richards_permeability: list[WillisRichardsPermeabilityType] = field( + default_factory=list, + metadata={ + "name": "WillisRichardsPermeability", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class ElasticFirstOrderSemtype: + class Meta: + name = "ElasticFirstOrderSEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ElasticSemtype: + class Meta: + name = "ElasticSEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + dt_seismo_trace: str = field( + default="0", + metadata={ + "name": "dtSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + enable_lifo: str = field( + default="0", + metadata={ + "name": "enableLifo", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + forward: str = field( + default="1", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + lifo_on_device: str = field( + default="-80", + metadata={ + "name": "lifoOnDevice", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_on_host: str = field( + default="-80", + metadata={ + "name": "lifoOnHost", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + lifo_size: str = field( + default="2147483647", + metadata={ + "name": "lifoSize", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + linear_dasgeometry: str = field( + default="{{0}}", + metadata={ + "name": "linearDASGeometry", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + output_seismo_trace: str = field( + default="0", + metadata={ + "name": "outputSeismoTrace", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + receiver_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "receiverCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + ricker_order: str = field( + default="2", + metadata={ + "name": "rickerOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + save_fields: str = field( + default="0", + metadata={ + "name": "saveFields", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + shot_index: str = field( + default="0", + metadata={ + "name": "shotIndex", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + source_coordinates: str = field( + default="{{0}}", + metadata={ + "name": "sourceCoordinates", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + source_force: str = field( + default="{0,0,0}", + metadata={ + "name": "sourceForce", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + source_moment: str = field( + default="{1,1,1,0,0,0}", + metadata={ + "name": "sourceMoment", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){5}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_source_delay: str = field( + default="-1", + metadata={ + "name": "timeSourceDelay", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_source_frequency: str = field( + default="0", + metadata={ + "name": "timeSourceFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ElementRegionsType: + cell_element_region: list[CellElementRegionType] = field( + default_factory=list, + metadata={ + "name": "CellElementRegion", + "type": "Element", + "namespace": "", + }, + ) + surface_element_region: list[SurfaceElementRegionType] = field( + default_factory=list, + metadata={ + "name": "SurfaceElementRegion", + "type": "Element", + "namespace": "", + }, + ) + well_element_region: list[WellElementRegionType] = field( + default_factory=list, + metadata={ + "name": "WellElementRegion", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class EmbeddedSurfaceGeneratorType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + fracture_region: str = field( + default="FractureRegion", + metadata={ + "name": "fractureRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mpi_comm_order: str = field( + default="0", + metadata={ + "name": "mpiCommOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_objects: Optional[str] = field( + default=None, + metadata={ + "name": "targetObjects", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class FieldSpecificationsType: + aquifer: list[AquiferType] = field( + default_factory=list, + metadata={ + "name": "Aquifer", + "type": "Element", + "namespace": "", + }, + ) + dirichlet: list[DirichletType] = field( + default_factory=list, + metadata={ + "name": "Dirichlet", + "type": "Element", + "namespace": "", + }, + ) + field_specification: list[FieldSpecificationType] = field( + default_factory=list, + metadata={ + "name": "FieldSpecification", + "type": "Element", + "namespace": "", + }, + ) + hydrostatic_equilibrium: list[HydrostaticEquilibriumType] = field( + default_factory=list, + metadata={ + "name": "HydrostaticEquilibrium", + "type": "Element", + "namespace": "", + }, + ) + pml: list[Pmltype] = field( + default_factory=list, + metadata={ + "name": "PML", + "type": "Element", + "namespace": "", + }, + ) + source_flux: list[SourceFluxType] = field( + default_factory=list, + metadata={ + "name": "SourceFlux", + "type": "Element", + "namespace": "", + }, + ) + traction: list[TractionType] = field( + default_factory=list, + metadata={ + "name": "Traction", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class FiniteElementsType: + finite_element_space: list[FiniteElementSpaceType] = field( + default_factory=list, + metadata={ + "name": "FiniteElementSpace", + "type": "Element", + "namespace": "", + }, + ) + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class FiniteVolumeType: + hybrid_mimetic_discretization: list[HybridMimeticDiscretizationType] = field( + default_factory=list, + metadata={ + "name": "HybridMimeticDiscretization", + "type": "Element", + "namespace": "", + }, + ) + two_point_flux_approximation: list[TwoPointFluxApproximationType] = field( + default_factory=list, + metadata={ + "name": "TwoPointFluxApproximation", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class FlowProppantTransportType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + proppant_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "proppantSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class FunctionsType: + composite_function: list[CompositeFunctionType] = field( + default_factory=list, + metadata={ + "name": "CompositeFunction", + "type": "Element", + "namespace": "", + }, + ) + multivariable_table_function: list[MultivariableTableFunctionType] = field( + default_factory=list, + metadata={ + "name": "MultivariableTableFunction", + "type": "Element", + "namespace": "", + }, + ) + symbolic_function: list[SymbolicFunctionType] = field( + default_factory=list, + metadata={ + "name": "SymbolicFunction", + "type": "Element", + "namespace": "", + }, + ) + table_function: list[TableFunctionType] = field( + default_factory=list, + metadata={ + "name": "TableFunction", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class GeometryType: + box: list[BoxType] = field( + default_factory=list, + metadata={ + "name": "Box", + "type": "Element", + "namespace": "", + }, + ) + custom_polar_object: list[CustomPolarObjectType] = field( + default_factory=list, + metadata={ + "name": "CustomPolarObject", + "type": "Element", + "namespace": "", + }, + ) + cylinder: list[CylinderType] = field( + default_factory=list, + metadata={ + "name": "Cylinder", + "type": "Element", + "namespace": "", + }, + ) + disc: list[DiscType] = field( + default_factory=list, + metadata={ + "name": "Disc", + "type": "Element", + "namespace": "", + }, + ) + rectangle: list[RectangleType] = field( + default_factory=list, + metadata={ + "name": "Rectangle", + "type": "Element", + "namespace": "", + }, + ) + thick_plane: list[ThickPlaneType] = field( + default_factory=list, + metadata={ + "name": "ThickPlane", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class HydrofractureType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: Optional[str] = field( + default=None, + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_matrix_poroelastic: str = field( + default="0", + metadata={ + "name": "isMatrixPoroelastic", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class IncludedType: + file: list[FileType] = field( + default_factory=list, + metadata={ + "name": "File", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class InternalWellType: + perforation: list[PerforationType] = field( + default_factory=list, + metadata={ + "name": "Perforation", + "type": "Element", + "namespace": "", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + min_element_length: str = field( + default="0.001", + metadata={ + "name": "minElementLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_segment_length: str = field( + default="0.01", + metadata={ + "name": "minSegmentLength", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_elements_per_segment: Optional[str] = field( + default=None, + metadata={ + "name": "numElementsPerSegment", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + polyline_node_coords: Optional[str] = field( + default=None, + metadata={ + "name": "polylineNodeCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + polyline_segment_conn: Optional[str] = field( + default=None, + metadata={ + "name": "polylineSegmentConn", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*\}\s*", + }, + ) + radius: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + well_controls_name: Optional[str] = field( + default=None, + metadata={ + "name": "wellControlsName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + well_region_name: Optional[str] = field( + default=None, + metadata={ + "name": "wellRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class LagrangianContactType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: Optional[str] = field( + default=None, + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + fracture_region_name: Optional[str] = field( + default=None, + metadata={ + "name": "fractureRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + stabilization_name: Optional[str] = field( + default=None, + metadata={ + "name": "stabilizationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class LaplaceFemtype: + class Meta: + name = "LaplaceFEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_integration_option: Optional[str] = field( + default=None, + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|SteadyState|ImplicitTransient", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class MultiphasePoromechanicsReservoirType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + well_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class MultiphasePoromechanicsType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + stabilization_multiplier: str = field( + default="1", + metadata={ + "name": "stabilizationMultiplier", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stabilization_region_names: str = field( + default="{}", + metadata={ + "name": "stabilizationRegionNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + stabilization_type: str = field( + default="None", + metadata={ + "name": "stabilizationType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|None|Global|Local", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class OutputsType: + blueprint: list[BlueprintType] = field( + default_factory=list, + metadata={ + "name": "Blueprint", + "type": "Element", + "namespace": "", + }, + ) + chombo_io: list[ChomboIotype] = field( + default_factory=list, + metadata={ + "name": "ChomboIO", + "type": "Element", + "namespace": "", + }, + ) + python: list[PythonType] = field( + default_factory=list, + metadata={ + "name": "Python", + "type": "Element", + "namespace": "", + }, + ) + restart: list[RestartType] = field( + default_factory=list, + metadata={ + "name": "Restart", + "type": "Element", + "namespace": "", + }, + ) + silo: list[SiloType] = field( + default_factory=list, + metadata={ + "name": "Silo", + "type": "Element", + "namespace": "", + }, + ) + time_history: list[TimeHistoryType] = field( + default_factory=list, + metadata={ + "name": "TimeHistory", + "type": "Element", + "namespace": "", + }, + ) + vtk: list[Vtktype] = field( + default_factory=list, + metadata={ + "name": "VTK", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class ParametersType: + parameter: list[ParameterType] = field( + default_factory=list, + metadata={ + "name": "Parameter", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class ParticleRegionsType: + particle_region: list[ParticleRegionType] = field( + default_factory=list, + metadata={ + "name": "ParticleRegion", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class PeriodicEventType: + halt_event: list["HaltEventType"] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: list["PeriodicEventType"] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: list[SoloEventType] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cycle_frequency: str = field( + default="1", + metadata={ + "name": "cycleFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + function: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + object_value: Optional[str] = field( + default=None, + metadata={ + "name": "object", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + set: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + stat: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_exact_timestep: str = field( + default="1", + metadata={ + "name": "targetExactTimestep", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + threshold: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_frequency: str = field( + default="-1", + metadata={ + "name": "timeFrequency", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PhaseFieldDamageFemtype: + class Meta: + name = "PhaseFieldDamageFEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + damage_upper_bound: str = field( + default="1.5", + metadata={ + "name": "damageUpperBound", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + field_name: Optional[str] = field( + default=None, + metadata={ + "name": "fieldName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + irreversibility_flag: str = field( + default="0", + metadata={ + "name": "irreversibilityFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + local_dissipation: Optional[str] = field( + default=None, + metadata={ + "name": "localDissipation", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|Linear|Quadratic", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_integration_option: Optional[str] = field( + default=None, + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|SteadyState|ImplicitTransient|ExplicitTransient", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class PhaseFieldFractureType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + damage_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "damageSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ProppantTransportType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + bridging_factor: str = field( + default="0", + metadata={ + "name": "bridgingFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + critical_shields_number: str = field( + default="0", + metadata={ + "name": "criticalShieldsNumber", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + friction_coefficient: str = field( + default="0.03", + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_proppant_concentration: str = field( + default="0.6", + metadata={ + "name": "maxProppantConcentration", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_density: str = field( + default="2500", + metadata={ + "name": "proppantDensity", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + proppant_diameter: str = field( + default="0.0004", + metadata={ + "name": "proppantDiameter", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + update_proppant_packing: str = field( + default="0", + metadata={ + "name": "updateProppantPacking", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class ReactiveCompositionalMultiphaseObltype: + class Meta: + name = "ReactiveCompositionalMultiphaseOBLType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + obloperators_table_file: Optional[str] = field( + default=None, + metadata={ + "name": "OBLOperatorsTableFile", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + allow_local_oblchopping: str = field( + default="1", + metadata={ + "name": "allowLocalOBLChopping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + component_names: str = field( + default="{}", + metadata={ + "name": "componentNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + enable_energy_balance: Optional[str] = field( + default=None, + metadata={ + "name": "enableEnergyBalance", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_comp_fraction_change: str = field( + default="1", + metadata={ + "name": "maxCompFractionChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + num_components: Optional[str] = field( + default=None, + metadata={ + "name": "numComponents", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + num_phases: Optional[str] = field( + default=None, + metadata={ + "name": "numPhases", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + phase_names: str = field( + default="{}", + metadata={ + "name": "phaseNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + trans_mult_exp: str = field( + default="1", + metadata={ + "name": "transMultExp", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + use_dartsl2_norm: str = field( + default="1", + metadata={ + "name": "useDARTSL2Norm", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseFvmtype: + class Meta: + name = "SinglePhaseFVMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseHybridFvmtype: + class Meta: + name = "SinglePhaseHybridFVMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhasePoromechanicsConformingFracturesType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + lagrangian_contact_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "LagrangianContactSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhasePoromechanicsEmbeddedFracturesType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + fractures_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "fracturesSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhasePoromechanicsReservoirType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + poromechanics_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "poromechanicsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + well_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhasePoromechanicsType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseProppantFvmtype: + class Meta: + name = "SinglePhaseProppantFVMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + allow_negative_pressure: str = field( + default="1", + metadata={ + "name": "allowNegativePressure", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_absolute_pressure_change: str = field( + default="-1", + metadata={ + "name": "maxAbsolutePressureChange", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + temperature: str = field( + default="0", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseReservoirPoromechanicsType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + is_thermal: str = field( + default="0", + metadata={ + "name": "isThermal", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reservoir_and_wells_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "reservoirAndWellsSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseReservoirType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + flow_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "flowSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + well_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "wellSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SinglePhaseWellType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + well_controls: list[WellControlsType] = field( + default_factory=list, + metadata={ + "name": "WellControls", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidMechanicsEmbeddedFracturesType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: Optional[str] = field( + default=None, + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + fracture_region_name: Optional[str] = field( + default=None, + metadata={ + "name": "fractureRegionName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + solid_solver_name: Optional[str] = field( + default=None, + metadata={ + "name": "solidSolverName", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + use_static_condensation: str = field( + default="0", + metadata={ + "name": "useStaticCondensation", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidMechanicsLagrangianSsletype: + class Meta: + name = "SolidMechanicsLagrangianSSLEType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + default="NOCONTACT", + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidMechanicsLagrangianFemtype: + class Meta: + name = "SolidMechanics_LagrangianFEMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_relation_name: str = field( + default="NOCONTACT", + metadata={ + "name": "contactRelationName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mass_damping: str = field( + default="0", + metadata={ + "name": "massDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_num_resolves: str = field( + default="10", + metadata={ + "name": "maxNumResolves", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + newmark_beta: str = field( + default="0.25", + metadata={ + "name": "newmarkBeta", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + newmark_gamma: str = field( + default="0.5", + metadata={ + "name": "newmarkGamma", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + stiffness_damping: str = field( + default="0", + metadata={ + "name": "stiffnessDamping", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + strain_theory: str = field( + default="0", + metadata={ + "name": "strainTheory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_generator_name: Optional[str] = field( + default=None, + metadata={ + "name": "surfaceGeneratorName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^,\{\}\s]*\s*", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SolidMechanicsMpmtype: + class Meta: + name = "SolidMechanics_MPMType" + + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + boundary_condition_types: str = field( + default="{0}", + metadata={ + "name": "boundaryConditionTypes", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + box_average_history: str = field( + default="0", + metadata={ + "name": "boxAverageHistory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + contact_gap_correction: str = field( + default="0", + metadata={ + "name": "contactGapCorrection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + cpdi_domain_scaling: str = field( + default="0", + metadata={ + "name": "cpdiDomainScaling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + damage_field_partitioning: str = field( + default="0", + metadata={ + "name": "damageFieldPartitioning", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + discretization: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + f_table_interp_type: str = field( + default="0", + metadata={ + "name": "fTableInterpType", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + f_table_path: Optional[str] = field( + default=None, + metadata={ + "name": "fTablePath", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + friction_coefficient: str = field( + default="0", + metadata={ + "name": "frictionCoefficient", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + needs_neighbor_list: str = field( + default="0", + metadata={ + "name": "needsNeighborList", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + neighbor_radius: str = field( + default="-1", + metadata={ + "name": "neighborRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + plane_strain: str = field( + default="0", + metadata={ + "name": "planeStrain", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + prescribed_bc_table: str = field( + default="0", + metadata={ + "name": "prescribedBcTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + prescribed_boundary_ftable: str = field( + default="0", + metadata={ + "name": "prescribedBoundaryFTable", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + reaction_history: str = field( + default="0", + metadata={ + "name": "reactionHistory", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + separability_min_damage: str = field( + default="0.5", + metadata={ + "name": "separabilityMinDamage", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + solver_profiling: str = field( + default="0", + metadata={ + "name": "solverProfiling", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + surface_detection: str = field( + default="0", + metadata={ + "name": "surfaceDetection", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + time_integration_option: str = field( + default="ExplicitDynamic", + metadata={ + "name": "timeIntegrationOption", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|QuasiStatic|ImplicitDynamic|ExplicitDynamic", + }, + ) + treat_fully_damaged_as_single_field: str = field( + default="1", + metadata={ + "name": "treatFullyDamagedAsSingleField", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_damage_as_surface_flag: str = field( + default="0", + metadata={ + "name": "useDamageAsSurfaceFlag", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class SurfaceGeneratorType: + linear_solver_parameters: list[LinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "LinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + nonlinear_solver_parameters: list[NonlinearSolverParametersType] = field( + default_factory=list, + metadata={ + "name": "NonlinearSolverParameters", + "type": "Element", + "namespace": "", + }, + ) + cfl_factor: str = field( + default="0.5", + metadata={ + "name": "cflFactor", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + fracture_region: str = field( + default="Fracture", + metadata={ + "name": "fractureRegion", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + initial_dt: str = field( + default="1e+99", + metadata={ + "name": "initialDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + mpi_comm_order: str = field( + default="0", + metadata={ + "name": "mpiCommOrder", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + node_based_sif: str = field( + default="0", + metadata={ + "name": "nodeBasedSIF", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + rock_toughness: Optional[str] = field( + default=None, + metadata={ + "name": "rockToughness", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target_regions: Optional[str] = field( + default=None, + metadata={ + "name": "targetRegions", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class TasksType: + compositional_multiphase_reservoir_poromechanics_initialization: list[ + CompositionalMultiphaseReservoirPoromechanicsInitializationType + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoirPoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_statistics: list[ + CompositionalMultiphaseStatisticsType + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseStatistics", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics_initialization: list[ + MultiphasePoromechanicsInitializationType + ] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + pvtdriver: list[PvtdriverType] = field( + default_factory=list, + metadata={ + "name": "PVTDriver", + "type": "Element", + "namespace": "", + }, + ) + pack_collection: list[PackCollectionType] = field( + default_factory=list, + metadata={ + "name": "PackCollection", + "type": "Element", + "namespace": "", + }, + ) + reactive_fluid_driver: list[ReactiveFluidDriverType] = field( + default_factory=list, + metadata={ + "name": "ReactiveFluidDriver", + "type": "Element", + "namespace": "", + }, + ) + relperm_driver: list[RelpermDriverType] = field( + default_factory=list, + metadata={ + "name": "RelpermDriver", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_initialization: list[ + SinglePhasePoromechanicsInitializationType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir_poromechanics_initialization: list[ + SinglePhaseReservoirPoromechanicsInitializationType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoirPoromechanicsInitialization", + "type": "Element", + "namespace": "", + }, + ) + single_phase_statistics: list[SinglePhaseStatisticsType] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseStatistics", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_state_reset: list[SolidMechanicsStateResetType] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsStateReset", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_statistics: list[SolidMechanicsStatisticsType] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsStatistics", + "type": "Element", + "namespace": "", + }, + ) + triaxial_driver: list[TriaxialDriverType] = field( + default_factory=list, + metadata={ + "name": "TriaxialDriver", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class CrusherType: + class Meta: + name = "crusherType" + + run: list[RunType] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class LassenType: + class Meta: + name = "lassenType" + + run: list[RunType] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class QuartzType: + class Meta: + name = "quartzType" + + run: list[RunType] = field( + default_factory=list, + metadata={ + "name": "Run", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class BenchmarksType: + crusher: list[CrusherType] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + lassen: list[LassenType] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + quartz: list[QuartzType] = field( + default_factory=list, + metadata={ + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class HaltEventType: + halt_event: list["HaltEventType"] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: list[PeriodicEventType] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: list[SoloEventType] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + begin_time: str = field( + default="0", + metadata={ + "name": "beginTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + end_time: str = field( + default="1e+100", + metadata={ + "name": "endTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + final_dt_stretch: str = field( + default="0.001", + metadata={ + "name": "finalDtStretch", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + force_dt: str = field( + default="-1", + metadata={ + "name": "forceDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_event_dt: str = field( + default="-1", + metadata={ + "name": "maxEventDt", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + max_runtime: Optional[str] = field( + default=None, + metadata={ + "name": "maxRuntime", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + target: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + target_exact_start_stop: str = field( + default="1", + metadata={ + "name": "targetExactStartStop", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class InternalMeshType: + internal_well: list[InternalWellType] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + cell_block_names: Optional[str] = field( + default=None, + metadata={ + "name": "cellBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + element_types: Optional[str] = field( + default=None, + metadata={ + "name": "elementTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + nx: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + ny: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + nz: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + position_tolerance: str = field( + default="1e-10", + metadata={ + "name": "positionTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + triangle_pattern: str = field( + default="0", + metadata={ + "name": "trianglePattern", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + x_bias: str = field( + default="{1}", + metadata={ + "name": "xBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + x_coords: Optional[str] = field( + default=None, + metadata={ + "name": "xCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_bias: str = field( + default="{1}", + metadata={ + "name": "yBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_coords: Optional[str] = field( + default=None, + metadata={ + "name": "yCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_bias: str = field( + default="{1}", + metadata={ + "name": "zBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_coords: Optional[str] = field( + default=None, + metadata={ + "name": "zCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class InternalWellboreType: + internal_well: list[InternalWellType] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + auto_space_radial_elems: str = field( + default="{-1}", + metadata={ + "name": "autoSpaceRadialElems", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + cartesian_mapping_inner_radius: str = field( + default="1e+99", + metadata={ + "name": "cartesianMappingInnerRadius", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + cell_block_names: Optional[str] = field( + default=None, + metadata={ + "name": "cellBlockNames", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + element_types: Optional[str] = field( + default=None, + metadata={ + "name": "elementTypes", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([^,\{\}\s]+\s*,\s*)*[^,\{\}\s]+\s*)?\}\s*", + }, + ) + hard_radial_coords: str = field( + default="{0}", + metadata={ + "name": "hardRadialCoords", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + nr: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + nt: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + nz: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]+\s*,\s*)*[+-]?[\d]+\s*)?\}\s*", + }, + ) + position_tolerance: str = field( + default="1e-10", + metadata={ + "name": "positionTolerance", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + r_bias: str = field( + default="{-0.8}", + metadata={ + "name": "rBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + radius: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + theta: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + trajectory: str = field( + default="{{0}}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*,\s*)*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*\}\s*", + }, + ) + triangle_pattern: str = field( + default="0", + metadata={ + "name": "trianglePattern", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + use_cartesian_outer_boundary: str = field( + default="1000000", + metadata={ + "name": "useCartesianOuterBoundary", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + x_bias: str = field( + default="{1}", + metadata={ + "name": "xBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + y_bias: str = field( + default="{1}", + metadata={ + "name": "yBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_bias: str = field( + default="{1}", + metadata={ + "name": "zBias", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + z_coords: Optional[str] = field( + default=None, + metadata={ + "name": "zCoords", + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|\s*\{\s*(([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*)*[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*)?\}\s*", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class NumericalMethodsType: + finite_elements: list[FiniteElementsType] = field( + default_factory=list, + metadata={ + "name": "FiniteElements", + "type": "Element", + "namespace": "", + }, + ) + finite_volume: list[FiniteVolumeType] = field( + default_factory=list, + metadata={ + "name": "FiniteVolume", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class SolversType: + acoustic_first_order_sem: list[AcousticFirstOrderSemtype] = field( + default_factory=list, + metadata={ + "name": "AcousticFirstOrderSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_sem: list[AcousticSemtype] = field( + default_factory=list, + metadata={ + "name": "AcousticSEM", + "type": "Element", + "namespace": "", + }, + ) + acoustic_vtisem: list[AcousticVtisemtype] = field( + default_factory=list, + metadata={ + "name": "AcousticVTISEM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_fvm: list[CompositionalMultiphaseFvmtype] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseFVM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_hybrid_fvm: list[ + CompositionalMultiphaseHybridFvmtype + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseHybridFVM", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_reservoir: list[ + CompositionalMultiphaseReservoirType + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoir", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_reservoir_poromechanics: list[ + CompositionalMultiphaseReservoirPoromechanicsType + ] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseReservoirPoromechanics", + "type": "Element", + "namespace": "", + }, + ) + compositional_multiphase_well: list[CompositionalMultiphaseWellType] = field( + default_factory=list, + metadata={ + "name": "CompositionalMultiphaseWell", + "type": "Element", + "namespace": "", + }, + ) + elastic_first_order_sem: list[ElasticFirstOrderSemtype] = field( + default_factory=list, + metadata={ + "name": "ElasticFirstOrderSEM", + "type": "Element", + "namespace": "", + }, + ) + elastic_sem: list[ElasticSemtype] = field( + default_factory=list, + metadata={ + "name": "ElasticSEM", + "type": "Element", + "namespace": "", + }, + ) + embedded_surface_generator: list[EmbeddedSurfaceGeneratorType] = field( + default_factory=list, + metadata={ + "name": "EmbeddedSurfaceGenerator", + "type": "Element", + "namespace": "", + }, + ) + flow_proppant_transport: list[FlowProppantTransportType] = field( + default_factory=list, + metadata={ + "name": "FlowProppantTransport", + "type": "Element", + "namespace": "", + }, + ) + hydrofracture: list[HydrofractureType] = field( + default_factory=list, + metadata={ + "name": "Hydrofracture", + "type": "Element", + "namespace": "", + }, + ) + lagrangian_contact: list[LagrangianContactType] = field( + default_factory=list, + metadata={ + "name": "LagrangianContact", + "type": "Element", + "namespace": "", + }, + ) + laplace_fem: list[LaplaceFemtype] = field( + default_factory=list, + metadata={ + "name": "LaplaceFEM", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics: list[MultiphasePoromechanicsType] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanics", + "type": "Element", + "namespace": "", + }, + ) + multiphase_poromechanics_reservoir: list[ + MultiphasePoromechanicsReservoirType + ] = field( + default_factory=list, + metadata={ + "name": "MultiphasePoromechanicsReservoir", + "type": "Element", + "namespace": "", + }, + ) + phase_field_damage_fem: list[PhaseFieldDamageFemtype] = field( + default_factory=list, + metadata={ + "name": "PhaseFieldDamageFEM", + "type": "Element", + "namespace": "", + }, + ) + phase_field_fracture: list[PhaseFieldFractureType] = field( + default_factory=list, + metadata={ + "name": "PhaseFieldFracture", + "type": "Element", + "namespace": "", + }, + ) + proppant_transport: list[ProppantTransportType] = field( + default_factory=list, + metadata={ + "name": "ProppantTransport", + "type": "Element", + "namespace": "", + }, + ) + reactive_compositional_multiphase_obl: list[ + ReactiveCompositionalMultiphaseObltype + ] = field( + default_factory=list, + metadata={ + "name": "ReactiveCompositionalMultiphaseOBL", + "type": "Element", + "namespace": "", + }, + ) + single_phase_fvm: list[SinglePhaseFvmtype] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_hybrid_fvm: list[SinglePhaseHybridFvmtype] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseHybridFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics: list[SinglePhasePoromechanicsType] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanics", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_conforming_fractures: list[ + SinglePhasePoromechanicsConformingFracturesType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsConformingFractures", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_embedded_fractures: list[ + SinglePhasePoromechanicsEmbeddedFracturesType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsEmbeddedFractures", + "type": "Element", + "namespace": "", + }, + ) + single_phase_poromechanics_reservoir: list[ + SinglePhasePoromechanicsReservoirType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhasePoromechanicsReservoir", + "type": "Element", + "namespace": "", + }, + ) + single_phase_proppant_fvm: list[SinglePhaseProppantFvmtype] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseProppantFVM", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir: list[SinglePhaseReservoirType] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoir", + "type": "Element", + "namespace": "", + }, + ) + single_phase_reservoir_poromechanics: list[ + SinglePhaseReservoirPoromechanicsType + ] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseReservoirPoromechanics", + "type": "Element", + "namespace": "", + }, + ) + single_phase_well: list[SinglePhaseWellType] = field( + default_factory=list, + metadata={ + "name": "SinglePhaseWell", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_embedded_fractures: list[ + SolidMechanicsEmbeddedFracturesType + ] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsEmbeddedFractures", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrangian_ssle: list[SolidMechanicsLagrangianSsletype] = field( + default_factory=list, + metadata={ + "name": "SolidMechanicsLagrangianSSLE", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_lagrangian_fem: list[SolidMechanicsLagrangianFemtype] = field( + default_factory=list, + metadata={ + "name": "SolidMechanics_LagrangianFEM", + "type": "Element", + "namespace": "", + }, + ) + solid_mechanics_mpm: list[SolidMechanicsMpmtype] = field( + default_factory=list, + metadata={ + "name": "SolidMechanics_MPM", + "type": "Element", + "namespace": "", + }, + ) + surface_generator: list[SurfaceGeneratorType] = field( + default_factory=list, + metadata={ + "name": "SurfaceGenerator", + "type": "Element", + "namespace": "", + }, + ) + gravity_vector: str = field( + default="{0,0,-9.81}", + metadata={ + "name": "gravityVector", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + + +@dataclass +class VtkmeshType: + class Meta: + name = "VTKMeshType" + + internal_well: list[InternalWellType] = field( + default_factory=list, + metadata={ + "name": "InternalWell", + "type": "Element", + "namespace": "", + }, + ) + face_blocks: str = field( + default="{}", + metadata={ + "name": "faceBlocks", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + field_names_in_geosx: str = field( + default="{}", + metadata={ + "name": "fieldNamesInGEOSX", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + fields_to_import: str = field( + default="{}", + metadata={ + "name": "fieldsToImport", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + file: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[^*?<>\|:\";,\s]*\s*", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + main_block_name: str = field( + default="main", + metadata={ + "name": "mainBlockName", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + nodeset_names: str = field( + default="{}", + metadata={ + "name": "nodesetNames", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + partition_method: str = field( + default="parmetis", + metadata={ + "name": "partitionMethod", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|parmetis|ptscotch", + }, + ) + partition_refinement: str = field( + default="1", + metadata={ + "name": "partitionRefinement", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + region_attribute: str = field( + default="attribute", + metadata={ + "name": "regionAttribute", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_/]*", + }, + ) + scale: str = field( + default="{1,1,1}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + surfacic_fields_in_geosx: str = field( + default="{}", + metadata={ + "name": "surfacicFieldsInGEOSX", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + surfacic_fields_to_import: str = field( + default="{}", + metadata={ + "name": "surfacicFieldsToImport", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*(([a-zA-Z0-9.\-_/]*\s*,\s*)*[a-zA-Z0-9.\-_/]*\s*)?\}\s*", + }, + ) + translate: str = field( + default="{0,0,0}", + metadata={ + "type": "Attribute", + "pattern": r".*[\[\]`$].*|\s*\{\s*([+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*,\s*){2}[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)\s*\}\s*", + }, + ) + use_global_ids: str = field( + default="0", + metadata={ + "name": "useGlobalIds", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + name: Optional[str] = field( + default=None, + metadata={ + "type": "Attribute", + "required": True, + "pattern": r".*[\[\]`$].*|[a-zA-Z0-9.\-_]+", + }, + ) + + +@dataclass +class EventsType: + halt_event: list[HaltEventType] = field( + default_factory=list, + metadata={ + "name": "HaltEvent", + "type": "Element", + "namespace": "", + }, + ) + periodic_event: list[PeriodicEventType] = field( + default_factory=list, + metadata={ + "name": "PeriodicEvent", + "type": "Element", + "namespace": "", + }, + ) + solo_event: list[SoloEventType] = field( + default_factory=list, + metadata={ + "name": "SoloEvent", + "type": "Element", + "namespace": "", + }, + ) + log_level: str = field( + default="0", + metadata={ + "name": "logLevel", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_cycle: str = field( + default="2147483647", + metadata={ + "name": "maxCycle", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]+", + }, + ) + max_time: real64 = field( + default=1.79769e308, + metadata={ + "name": "maxTime", + "type": "Attribute", + # "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + min_time: str = field( + default="0", + metadata={ + "name": "minTime", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|[+-]?[\d]*([\d]\.?|\.[\d])[\d]*([eE][-+]?[\d]+|\s*)", + }, + ) + time_output_format: str = field( + default="seconds", + metadata={ + "name": "timeOutputFormat", + "type": "Attribute", + "pattern": r".*[\[\]`$].*|seconds|minutes|hours|days|years|full", + }, + ) + + +@dataclass +class MeshType: + internal_mesh: list[InternalMeshType] = field( + default_factory=list, + metadata={ + "name": "InternalMesh", + "type": "Element", + "namespace": "", + }, + ) + internal_wellbore: list[InternalWellboreType] = field( + default_factory=list, + metadata={ + "name": "InternalWellbore", + "type": "Element", + "namespace": "", + }, + ) + particle_mesh: list[ParticleMeshType] = field( + default_factory=list, + metadata={ + "name": "ParticleMesh", + "type": "Element", + "namespace": "", + }, + ) + vtkmesh: list[VtkmeshType] = field( + default_factory=list, + metadata={ + "name": "VTKMesh", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class ProblemType: + events: list[EventsType] = field( + default_factory=list, + metadata={ + "name": "Events", + "type": "Element", + "namespace": "", + }, + ) + field_specifications: list[FieldSpecificationsType] = field( + default_factory=list, + metadata={ + "name": "FieldSpecifications", + "type": "Element", + "namespace": "", + }, + ) + functions: list[FunctionsType] = field( + default_factory=list, + metadata={ + "name": "Functions", + "type": "Element", + "namespace": "", + }, + ) + geometry: list[GeometryType] = field( + default_factory=list, + metadata={ + "name": "Geometry", + "type": "Element", + "namespace": "", + }, + ) + mesh: list[MeshType] = field( + default_factory=list, + metadata={ + "name": "Mesh", + "type": "Element", + "namespace": "", + }, + ) + numerical_methods: list[NumericalMethodsType] = field( + default_factory=list, + metadata={ + "name": "NumericalMethods", + "type": "Element", + "namespace": "", + }, + ) + outputs: list[OutputsType] = field( + default_factory=list, + metadata={ + "name": "Outputs", + "type": "Element", + "namespace": "", + }, + ) + solvers: list[SolversType] = field( + default_factory=list, + metadata={ + "name": "Solvers", + "type": "Element", + "namespace": "", + }, + ) + tasks: list[TasksType] = field( + default_factory=list, + metadata={ + "name": "Tasks", + "type": "Element", + "namespace": "", + }, + ) + constitutive: list[ConstitutiveType] = field( + default_factory=list, + metadata={ + "name": "Constitutive", + "type": "Element", + "namespace": "", + }, + ) + element_regions: list[ElementRegionsType] = field( + default_factory=list, + metadata={ + "name": "ElementRegions", + "type": "Element", + "namespace": "", + }, + ) + particle_regions: list[ParticleRegionsType] = field( + default_factory=list, + metadata={ + "name": "ParticleRegions", + "type": "Element", + "namespace": "", + }, + ) + included: list[IncludedType] = field( + default_factory=list, + metadata={ + "name": "Included", + "type": "Element", + "namespace": "", + }, + ) + parameters: list[ParametersType] = field( + default_factory=list, + metadata={ + "name": "Parameters", + "type": "Element", + "namespace": "", + }, + ) + benchmarks: list[BenchmarksType] = field( + default_factory=list, + metadata={ + "name": "Benchmarks", + "type": "Element", + "namespace": "", + }, + ) + + +@dataclass +class Problem(ProblemType): + pass diff --git a/geos-xml-viewer/src/geos_xml_viewer/geos/models/test.py b/geos-xml-viewer/src/geos_xml_viewer/geos/models/test.py new file mode 100644 index 00000000..c6314153 --- /dev/null +++ b/geos-xml-viewer/src/geos_xml_viewer/geos/models/test.py @@ -0,0 +1,102 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +from dataclasses import dataclass + +import numpy as np +from xsdata.formats.converter import Converter, converter + + +@dataclass +class integer: + value: np.int32 + + +class integerConverter(Converter): + def deserialize(self, value: str, **kwargs) -> integer: + return integer(value) + + def serialize(self, value: integer, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(integer, integerConverter()) + + +@dataclass +class real32: + value: np.float32 + + +class real32Converter(Converter): + def deserialize(self, value: str, **kwargs) -> real32: + return real32(value) + + def serialize(self, value: real32, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(real32, real32Converter()) + + +@dataclass +class real64: + value: np.float64 + + +class real64Converter(Converter): + def deserialize(self, value: str, **kwargs) -> real64: + print("deserialize") + return real64(value=np.float64(value)) + + def serialize(self, value: real64, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(real64, real64Converter()) + + +@dataclass +class globalIndex: + value: np.int64 + + +class globalIndexConverter(Converter): + def deserialize(self, value: str, **kwargs) -> globalIndex: + return globalIndex(value) + + def serialize(self, value: globalIndex, **kwargs) -> str: + if kwargs["format"]: + return kwargs["format"].format(value) + return str(value) + + +converter.register_converter(globalIndex, globalIndexConverter()) + + +def custom_class_factory(clazz, params): + if clazz is real64: + return clazz(**{k: v for k, v in params.items()}) + + return clazz(**params) + + +# @dataclass +# class globalIndex_array: +# value: np.ndarray[np.int64] + +# class globalIndex_arrayConverter(Converter): +# def deserialize(self, value: str, **kwargs) -> globalIndex_array: +# return globalIndex_array(value) + +# def serialize(self, value: globalIndex_array, **kwargs) -> str: +# if kwargs["format"]: +# return kwargs["format"].format(value) +# return str(value) diff --git a/geos-xml-viewer/src/geos_xml_viewer/py.typed b/geos-xml-viewer/src/geos_xml_viewer/py.typed new file mode 100644 index 00000000..e69de29b diff --git a/geos-xml-viewer/tests/__init__.py b/geos-xml-viewer/tests/__init__.py new file mode 100644 index 00000000..ffa33702 --- /dev/null +++ b/geos-xml-viewer/tests/__init__.py @@ -0,0 +1,4 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + diff --git a/geos-xml-viewer/tests/files/connection.json b/geos-xml-viewer/tests/files/connection.json new file mode 100644 index 00000000..52db0eb0 --- /dev/null +++ b/geos-xml-viewer/tests/files/connection.json @@ -0,0 +1,762 @@ +{ + "P1.None.000.040.040.001": { + "w": "P1", + "l": [ + null, + 0 + ], + "g": [ + 40, + 40, + 1 + ], + "kh": 0, + "t": 0, + "x": [ + 19.75, + 19.75, + 0.25 + ] + }, + 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 + + + BQAAAAAAAAAAgAAAAAAAABUTAAAAAAAAhAAAAAAAAACEAAAAAAAAAIQAAAAAAAAAhAAAAAAAAABgAAAAAAAAAA==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 + + + + + diff --git a/geos-xml-viewer/tests/test_deckSource.py b/geos-xml-viewer/tests/test_deckSource.py new file mode 100644 index 00000000..78a5bea6 --- /dev/null +++ b/geos-xml-viewer/tests/test_deckSource.py @@ -0,0 +1,26 @@ +# SPDX-License-Identifier: Apache-2.0 +# SPDX-FileCopyrightText: Copyright 2023-2024 TotalEnergies. +# SPDX-FileContributor: Lionel Untereiner + +from pathlib import Path + +from geos_xml_viewer.filters.geosDeckReader import GeosDeckReader + +# Dir containing the files +FIXTURE_DIR = Path(__file__).parent.resolve() / "files" + + +# @pytest.mark.datafiles(FIXTURE_DIR / "singlePhaseFlow") +def test_DeckReader() -> None: + """Test the DeckReader.""" + datafile = Path("singlePhaseFlow/FieldCaseTutorial3_smoke.xml") + path = str(FIXTURE_DIR / datafile) + reader = GeosDeckReader() + reader.SetFileName(path) + reader.SetAttributeName("attribute") + reader.Update() + assert ( + reader.GetOutputDataObject(0).GetClassName() + == "vtkPartitionedDataSetCollection" + ) + assert reader.GetOutputDataObject(0).GetNumberOfPartitionedDataSets() == 5